阅读说明：本技术 一种改性丝光沸石分子筛及其制备方法 (Modified mordenite molecular sieve and preparation method thereof ) 是由 刘荣升 刘中民 于政锡 王莹利 于 2019-08-22 设计创作，主要内容包括：本申请公开了一种改性丝光沸石分子筛及其制备方法,所述改性丝光沸石分子筛中十二元环的酸性位数≤0.2mmol/g时,侧口袋酸性位数≥0.2mmol/g；所述改性丝光沸石分子筛的制备方法包括：获得Na-MOR分子筛；将所述Na-MOR分子筛采用四氯化硅进行同晶置换反应,得到前驱体；将前驱体进行铵离子交换,焙烧,得到所述改性丝光沸石分子筛。所述方法可以选择性的在丝光沸石外表面和十二元环孔道中发生同晶置换反应,进行脱铝补硅改性,从而定向消除分子筛外表面和十二元环孔道中的酸性位,八元环孔道内的酸性位活性继续保持。(The application discloses a modified mordenite molecular sieve and a preparation method thereof, wherein when the acid figure of a twelve-membered ring in the modified mordenite molecular sieve is less than or equal to 0.2mmol/g, the acid figure of a side pocket is more than or equal to 0.2 mmol/g; the preparation method of the modified mordenite molecular sieve comprises the following steps: obtaining Na-MOR molecular sieve; carrying out isomorphous replacement reaction on the Na-MOR molecular sieve by adopting silicon tetrachloride to obtain a precursor; and (3) performing ammonium ion exchange on the precursor, and roasting to obtain the modified mordenite molecular sieve. The method can selectively generate isomorphous replacement reaction on the outer surface of the mordenite and in the twelve-membered ring channel, and carry out dealumination and silicon supplementation modification, thereby directionally eliminating the acid sites on the outer surface of the molecular sieve and in the twelve-membered ring channel, and continuously maintaining the activity of the acid sites in the eight-membered ring channel.)

1. A modified mordenite molecular sieve is characterized in that when the acid figure of a twelve-membered ring in the modified mordenite molecular sieve is less than or equal to 0.2mmol/g, the acid figure of a side pocket is more than or equal to 0.2 mmol/g.

2. The modified mordenite zeolite molecular sieve of claim 1, wherein said modified mordenite zeolite molecular sieve has a twelve membered ring with an acid figure of 0.15mmol/g or less and a side pocket with an acid figure of 0.2mmol/g or more;

preferably, when the acid figure of the twelve-membered ring in the modified mordenite molecular sieve is 0.01-0.15 mmol/g, the acid figure of the side pocket is 0.2-0.3 mmol/g;

preferably, when the acid figure of the twelve-membered ring in the modified mordenite molecular sieve is 0.05-0.15 mmol/g, the acid figure of the side pocket is 0.2-0.3 mmol/g;

preferably, when the acid figure of the twelve-membered ring in the modified mordenite molecular sieve is 0.025-0.122 mmol/g, the acid figure of the side pocket is 0.229-0.276 mmol/g;

preferably, when the acid figure of the twelve-membered ring in the modified mordenite molecular sieve is 0.051-0.196 mmol/g, the acid figure of the side pocket is 0.238-0.283 mmol/g.

3. A process for the preparation of a modified mordenite molecular sieve as claimed in claim 1 or 2, wherein said modified mordenite molecular sieve is prepared by a process which comprises:

(1) obtaining Na-MOR molecular sieve;

(2) carrying out isomorphous replacement reaction on the Na-MOR molecular sieve in the step (1) by adopting silicon tetrachloride to obtain a precursor;

(3) performing ammonium ion exchange on the precursor in the step (2), and roasting to obtain the modified mordenite molecular sieve;

wherein, the Na-MOR molecular sieve is a mordenite molecular sieve, and cations in the mordenite molecular sieve are sodium ions.

4. The method of claim 3, wherein the Na-MOR molecular sieve in step (1) is obtained by a method comprising:

carrying out ion exchange on the mordenite molecular sieve to be treated to obtain a Na-MOR molecular sieve;

preferably, the ion exchange comprises: soaking the mordenite molecular sieve to be treated in a soluble sodium salt solution, and stirring to obtain a precursor; then roasting the precursor to obtain the Na-MOR molecular sieve;

preferably, the liquid-solid weight ratio of the mordenite molecular sieve to be treated immersed in the soluble sodium salt solution is 2-10;

the concentration of the soluble sodium salt solution is 0.01-1 mol/ml;

the stirring conditions are as follows: stirring for 1-4 hours at 40-90 ℃;

the roasting conditions are as follows: roasting at 450-600 ℃ for 2-6 hours.

5. The preparation method according to claim 3, wherein the Na-MOR molecular sieve is subjected to an activation treatment before isomorphous replacement in the step (2);

the activation conditions are as follows: and (3) activating at 400-600 ℃ in an inert atmosphere.

6. The preparation method according to claim 3, wherein the isomorphous substitution with silicon tetrachloride in step (2) comprises: reacting the Na-MOR molecular sieve to be treated in a mixed atmosphere containing saturated silicon tetrachloride saturated steam;

wherein the volume concentration of silicon tetrachloride saturated vapor in the mixed atmosphere is not more than 50%;

preferably, the reaction conditions are: the reaction temperature is 400-700 ℃, and the reaction time is 0.5-12 h;

preferably, the reaction is completed and then purged with an inert gas.

7. The preparation method according to claim 3, wherein after the isomorphous replacement reaction is completed, residual silicon tetrachloride in the system is completely removed.

8. The method according to claim 3, wherein the precursor in the step (2) is washed and then subjected to ammonium ion exchange.

9. The production method according to claim 3, wherein the conditions for the calcination in the step (3) include: roasting at 400-600 ℃ in an air atmosphere for 3-10 h.

10. The process of claim 3, wherein the modified mordenite molecular sieve is prepared by a process comprising:

1) fully exchanging the cations of the mordenite for sodium ions by ion exchange;

2) activating the mordenite molecular sieve obtained in the step 1) at the temperature of 400-600 ℃ in an inactive atmosphere, then performing dealumination and silicon supplementation modification on the mordenite molecular sieve obtained in the step 1) by adopting a silicon tetrachloride isomorphous replacement method under a reaction condition, and purging after the reaction is finished;

3) and (3) after purging, washing the molecular sieve, performing ammonium ion exchange, and roasting at 400-600 ℃ in an air atmosphere for 3-10h to obtain the modified mordenite molecular sieve.

Technical Field

The application relates to a modified mordenite molecular sieve and a preparation method thereof, belonging to the field of zeolite molecular sieves.

Background

The molecular sieve has unique acid property and pore channel structure, and may be used as shape selective catalyst widely in petrochemical process and chemical synthesis, and its shape selective catalytic performance is also affected mainly by surface acid site and pore channel structure. Therefore, the research on the acid site property and the distribution of the molecular sieve in different pore passages has important significance for the development and the application of the shape-selective catalyst. When the reaction performance of different pore channels in the multi-pore channel molecular sieve is researched, some modification means are needed to passivate the acid sites of other pore channels in advance.

The framework structure of the mordenite molecular sieve is that twelve-membered ring and eight-membered ring straight channels which are parallel exist along the [001] direction and are both oval, the eight-membered ring channel is positioned between the twelve-membered ring channels, the twelve-membered ring channel has the size of 0.65nm multiplied by 0.70nm, and the eight-membered ring channel has the size of 0.26nm multiplied by 0.57 nm. There is also an eight-membered ring straight channel along the [010] direction, called the side pocket, with channel dimensions of 0.34nm x 0.48 nm. According to research, in some small molecule reactions catalyzed by mordenite molecular sieves, small molecules have different reaction performances in eight-membered ring and twelve-membered ring channels. The activity of the acid site in the eight-membered ring channel is higher, the target product has better selectivity, and the acid site in the twelve-membered ring channel has a great relationship with the deactivation of the mordenite molecular sieve catalyst. Therefore, in order to improve the selectivity of the target product and the stability of the catalyst, the acid sites in the twelve-membered ring channels of the mordenite need to be selectively passivated to eliminate the effect of the acid sites in the twelve-membered ring channels in the reaction.

Patent CN101613274A discloses a method for preparing methyl acetate from dimethyl ether, which is to use pyridine organic amine to perform saturated adsorption on hydrogen mordenite, and a proper amount of alkaline molecules can effectively poison the acidic sites in the twelve-membered ring channels of mordenite, and retain the acidic sites in the eight-membered ring, thereby effectively inhibiting carbon deposition inactivation and simultaneously maintaining the catalytic activity. However, the molecular sieve has some disadvantages, such as easy removal of pyridine organic amine during the use process, resulting in the reduction of catalyst stability and methyl acetate selectivity.

Disclosure of Invention

According to one aspect of the present application, there is provided a modified mordenite molecular sieve having modulated acid number bits and side pocket acid number bits of a twelve membered ring; the method can selectively and permanently eliminate the acid sites on the inner and outer surfaces of the mordenite twelve-membered ring channels.

The method for modifying the mordenite molecular sieve specifically comprises the following steps: completely exchanging the molecular sieve to the sodium form; and (3) carrying out isomorphous replacement dealumination and silicon supplementation modification on the pretreated mordenite molecular sieve, washing the mordenite molecular sieve by using deionized water after finishing the isomorphous replacement dealumination and silicon supplementation modification, then carrying out ion exchange to a hydrogen type, and roasting to obtain the target molecular sieve.

The modified mordenite molecular sieve is characterized in that when the acid figure of a twelve-membered ring in the modified mordenite molecular sieve is less than or equal to 0.2mmol/g, the acid figure of a side pocket is more than or equal to 0.2 mmol/g.

The modified mordenite molecular sieve is characterized in that when the acid figure of a twelve-membered ring in the modified mordenite molecular sieve is less than or equal to 0.15mmol/g, the acid figure of a side pocket is more than or equal to 0.2 mmol/g.

Optionally, when the acid figure of the twelve-membered ring in the modified mordenite molecular sieve is 0.01-0.15 mmol/g, the acid figure of the side pocket is 0.2-0.3 mmol/g.

Optionally, when the acid number of the twelve-membered ring in the modified mordenite molecular sieve is 0.025-0.122 mmol/g, the acid number of the side pocket is 0.229-0.276 mmol/g.

Optionally, when the acid number of the twelve-membered ring in the modified mordenite molecular sieve is 0.005-0.122 mmol/g, the acid number of the side pocket is 0.185-0.276 mmol/g.

Optionally, when the acid number of the twelve-membered ring in the modified mordenite molecular sieve is 0.051-0.196 mmol/g, the acid number of the side pocket is 0.238-0.283 mmol/g.

In another aspect of the present application, there is provided a method for preparing the modified mordenite molecular sieve, wherein the method for preparing the modified mordenite molecular sieve comprises:

(1) obtaining Na-MOR molecular sieve;

(2) carrying out isomorphous replacement reaction on the Na-MOR molecular sieve in the step (1) by adopting silicon tetrachloride to obtain a precursor;

(3) performing ammonium ion exchange on the precursor in the step (2), and roasting to obtain the modified mordenite molecular sieve;

wherein, the Na-MOR molecular sieve is a mordenite molecular sieve, and cations in the mordenite molecular sieve are sodium ions.

Alternatively, in step (1), said Na-MOR molecular sieve is obtained in a manner comprising:

and (3) carrying out ion exchange on the mordenite molecular sieve to be treated to obtain the Na-MOR molecular sieve.

As a specific embodiment, the Na-MOR molecular sieve is obtained by the following steps: the cation of the mordenite was completely exchanged for sodium ion by ion exchange.

Alternatively, the mordenite molecular sieve to be treated which is ion-exchanged is a mordenite molecular sieve available in the art.

Optionally, the ion exchange comprises: soaking the mordenite molecular sieve to be treated in a soluble sodium salt solution, and stirring to obtain a precursor; and then roasting the precursor to obtain the Na-MOR molecular sieve.

Optionally, the liquid-solid weight ratio of the mordenite molecular sieve to be treated immersed in the soluble sodium salt solution is 2-10;

the concentration of the soluble sodium salt solution is 0.01-1 mol/ml;

the stirring conditions are as follows: stirring for 1-4 hours at 40-90 ℃;

the roasting conditions are as follows: roasting at 450-600 ℃ for 2-6 hours.

Optionally, the soluble sodium salt comprises at least one of sodium nitrate, sodium chloride, sodium acetate, sodium carbonate.

Optionally, in the ion exchange process, solid-liquid separation is performed after stirring, and then the mordenite sample is washed by deionized water until the solution is neutral, and then drying is performed; the drying conditions are as follows: drying at 70-120 ℃.

As a specific embodiment, the Na-MOR molecular sieve is obtained by the following steps:

(1) placing a mordenite sample in a soluble sodium salt solution with a certain concentration, wherein the liquid-solid ratio is 2-10 (weight ratio);

(2) stirring for 1-4 hours at 40-90 ℃;

(3) after solid-liquid separation, washing the mordenite sample by using deionized water until the solution is neutral;

(4) drying at 70-120 ℃, and then roasting at 450-600 ℃ for 2-6 hours to obtain the pretreated molecular sieve.

Optionally, the upper liquid-to-solid weight ratio limit is selected from 3, 4, 5, 6, 7, 8, 9, or 10; the lower limit is selected from 2, 3, 4, 5, 6, 7, 8 or 9.

Optionally, the upper temperature limit of the stirring is selected from 45 ℃, 50 ℃, 60 ℃, 70 ℃, 80 ℃ or 90 ℃; the lower limit is selected from 40 deg.C, 45 deg.C, 50 deg.C, 60 deg.C, 70 deg.C or 80 deg.C.

Optionally, the upper limit of time for the stirring is selected from 1.5 hours, 2 hours, 3 hours, or 4 hours; the lower limit is selected from 1 hour, 1.5 hours, 2 hours or 3 hours.

Optionally, the upper temperature limit of the calcination is selected from 500 ℃, 550 ℃, or 600 ℃; the lower limit is selected from 450 ℃, 500 ℃ or 550 ℃.

Optionally, the upper time limit for the calcination is selected from 3 hours, 4 hours, 5 hours, or 6 hours; the lower limit is selected from 2 hours, 3 hours, 4 hours or 5 hours.

Optionally, the Na-MOR molecular sieve is subjected to activation treatment before isomorphous replacement in the step (2);

the activation conditions are as follows: and (3) activating at 400-600 ℃ in an inert atmosphere.

Optionally, the inert atmosphere comprises at least one of nitrogen and an inert gas.

Optionally, the inert atmosphere comprises one of nitrogen and helium or a mixture of nitrogen and helium.

Optionally, the activation time is 1-5 hours.

Optionally, the upper temperature limit of the activation is selected from 500 ℃ or 600 ℃; the lower limit is selected from 400 ℃ or 500 ℃.

Optionally, the isomorphous replacement with silicon tetrachloride in step (2) includes: reacting the Na-MOR molecular sieve to be treated in a mixed atmosphere containing saturated silicon tetrachloride saturated steam;

wherein the volume concentration of silicon tetrachloride saturated vapor in the mixed atmosphere is not more than 50%.

Optionally, the mixed atmosphere further comprises an inert gas.

Optionally, the mixed atmosphere further comprises at least one of nitrogen and inert gas.

Optionally, the mixed atmosphere further includes at least one of nitrogen and helium.

Optionally, the upper limit of the volume concentration of silicon tetrachloride saturated vapor in the mixed atmosphere is selected from 5%, 10%, 20%, 30%, 40% or 50%; the lower limit is selected from 1%, 5%, 10%, 20%, 30% or 40%.

Optionally, the reaction conditions are: the reaction temperature is 400-700 ℃, and the reaction time is 0.5-12 h.

Optionally, the reaction conditions are: the reaction temperature is 400-700 ℃, and the reaction time is 0.5-6 h.

Optionally, the upper reaction temperature limit is selected from 450 ℃, 500 ℃, 550 ℃, 600 ℃, 650 ℃ or 700 ℃; the lower limit is selected from 400 deg.C, 450 deg.C, 500 deg.C, 550 deg.C, 600 deg.C or 650 deg.C.

Optionally, the upper reaction time limit is selected from 1h, 1.5h, 2h, 2.5h, 3h, 3.5h, 4h, 4.5h, 5h, 5.5h, 6h, 6.5h, 7h, 7.5h, 8h, 8.5h, 9h, 9.5h, 10h, 10.5h, 11h, 11.5h, or 12 h; the lower limit is selected from 0.5h, 1h, 1.5h, 2h, 2.5h, 3h, 3.5h, 4h, 4.5h, 5h, 5.5h, 6h, 6.5h, 7h, 7.5h, 8h, 8.5h, 9h, 9.5h, 10h, 10.5h, 11h or 11.5 h.

Optionally, the reaction is followed by a purge treatment with an inert gas.

Optionally, the inert gas comprises at least one of nitrogen and an inert gas.

Optionally, the inactive gas comprises one or a mixture of nitrogen and helium.

Optionally, after the isomorphous replacement reaction is completed, the residual silicon tetrachloride in the system is completely removed.

Alternatively, the molecular sieve should be sufficiently washed clean of the solid products remaining in the molecular sieve with deionized water after the isomorphous metathesis reaction.

Optionally, the precursor in step (2) is washed and then subjected to ammonium ion exchange.

Optionally, the ammonium ion exchange comprises: adding the substance to be treated to a solution containing NH₄ ⁺The solution of (2) is subjected to ammonium ion exchange.

Alternatively, the ammonium ion exchange may employ prior art ammonium ion exchange procedures and conditions, such as those employed in the prior art for ammonium ion exchange in mordenite molecular sieves.

As a specific embodiment, step (2) includes: introducing carrier gas into a reactor loaded with the molecular sieve for activation, then introducing mixed atmosphere carrying silicon tetrachloride saturated steam for reaction and adsorption, wherein the volume concentration of the silicon tetrachloride is 0-50%, and switching pure inactive gas to purge after adsorption saturation.

Alternatively, the conditions for the calcination in step (3) include: roasting at 400-600 ℃ in an air atmosphere for 3-10 h.

Optionally, the upper temperature limit of the calcination is selected from 500 ℃ or 600 ℃; the lower limit is selected from 400 ℃ or 500 ℃.

Optionally, the upper time limit for the calcination is selected from 4 hours, 5 hours, 6 hours, 7 hours, 8 hours, 9 hours, or 10 hours; the lower limit is selected from 3 hours, 4 hours, 5 hours, 6 hours, 7 hours, 8 hours, or 9 hours.

Optionally, the preparation method of the modified mordenite molecular sieve comprises the following steps:

1) fully exchanging the cations of the mordenite for sodium ions by ion exchange;

2) activating the mordenite molecular sieve obtained in the step 1) at the temperature of 400-600 ℃ in an inactive atmosphere, then performing dealumination and silicon supplementation modification on the mordenite molecular sieve obtained in the step 1) by adopting a silicon tetrachloride isomorphous replacement method under a reaction condition, and purging after the reaction is finished;

3) and (3) after purging, washing the molecular sieve, performing ammonium ion exchange, and roasting at 400-600 ℃ in an air atmosphere for 3-10h to obtain the modified mordenite molecular sieve.

As a specific embodiment, the preparation method of the modified mordenite molecular sieve comprises the following steps: firstly, completely exchanging the molecular sieve to a sodium type through sodium ion exchange, wherein the used solution is one of sodium nitrate, sodium chloride, sodium acetate, sodium carbonate and other sodium ion-containing solutions with certain concentration; and then carrying out silicon tetrachloride isomorphous replacement on the sodium mordenite molecular sieve at a certain temperature by adopting a chemical gas-solid phase reaction method to remove aluminum and supplement silicon for modification, firstly filling the molecular sieve in a quartz tube reactor, and then activating for 0.5-4 h at 400-600 ℃ in an inert atmosphere to remove impurities in the molecular sieve. (ii) a Adjusting the temperature to the temperature required by the isomorphous replacement reaction, starting the reaction, introducing a mixed gas of silicon tetrachloride and inert gas, wherein the volume concentration of the silicon tetrachloride is more than 0 and less than or equal to 50 percent, the preferred reaction temperature is 400-700 ℃, and the reaction time is 0.5-12 h. And after the reaction is finished, fully purging, purging impurities remained in the reaction tube and the molecular sieve, cooling, taking out the molecular sieve, washing the molecular sieve with deionized water for 6 times, and then exchanging ammonia ions to a hydrogen form to obtain the required molecular sieve catalyst.

Optionally, when the acid position of the twelve-membered ring in the modified mordenite molecular sieve obtained by the preparation method of the modified mordenite molecular sieve is as low as below 0.1mmol/g, the acid position of the side pocket is maintained above 0.2 mmol/g.

According to the method, isomorphous replacement reaction selectively occurs on the outer surface of the mordenite and in a twelve-membered ring channel, dealumination and silicon supplementation modification are performed, so that acid sites on the outer surface of the molecular sieve and in the twelve-membered ring channel are directionally eliminated, and when isomorphous replacement reaction occurs on the outer surface of the mordenite and in the twelve-membered ring channel, silicon tetrachloride cannot enter a side pocket to perform modification reaction because the molecular size of the silicon tetrachloride is larger than that of an eight-membered ring channel, so that the activity of the acid sites in the eight-membered ring channel is continuously maintained.

The mordenite 12-membered ring channel is a one-dimensional straight channel, so the restriction is serious by substance diffusion, the kinetic diameter of the silicon tetrachloride molecule is close to the size of the mordenite 12-membered ring channel, the silicon trichloride and the sodium tetrachloroaluminate which are products after isomorphous replacement reaction are both solids and are adsorbed in the channel to further influence the substance diffusion. The method described in the present application overcomes the technical problems of the prior art in limiting isomorphous replacement due to diffusion of species; meanwhile, silicon is supplemented by dealuminizing silicon tetrachloride to modify the silicon-containing silicon-: titanium atoms and the like, and has the advantages of completely passivating acid sites and not bringing new active sites.

The beneficial effects that this application can produce include:

the molecular sieve is modified by adopting a silicon tetrachloride dealuminization and silicon supplementation method, so that the acid sites in the inner and outer surfaces of a twelve-membered ring channel of the molecular sieve can be effectively eliminated, the acid sites in the side pocket channels of the mordenite molecular sieve can hardly be changed, and the size of the openings of the molecular sieve channels is only slightly influenced; the modified mordenite molecular sieve with a certain twelve-membered ring acidity figure and a side pocket acidity figure is prepared.

Drawings

FIG. 1 is a graph of the performance of the cumene cleavage reaction on mordenite for different isomorphous displacement modification times in examples 1 to 9;

figure 2 is a graph of the performance of the cumene cleavage reaction on mordenite at different isomorphous displacement modification temperatures for examples 16 to 22.

Detailed Description

The present application will be described in detail with reference to examples, but the present application is not limited to these examples.

Unless otherwise specified, the raw materials in the examples of the present application were all purchased commercially; in the embodiment, the Si/Al of the mordenite raw material is 10, and the particle size is 100-300 nm. H-MOR is hydrogen mordenite molecular sieve which is prepared by completely exchanging ammonium ions with mordenite raw material.

The analysis method in the examples of the present application is as follows:

acid site assay analysis was performed using a Bruker tenor 27 fourier infrared spectrometer in combination with probe molecular adsorption.

Elemental analysis was performed using an Axios type fluorescence spectrometer (XRF) from PANalytical.

In the examples of the present application, the cumene conversion was calculated by:

according to one embodiment of the application, the preparation method of the silicon tetrachloride isomorphous replacement modified mordenite molecular sieve comprises the following steps:

1) fully exchanging the cations of the mordenite for sodium ions by ion exchange;

2) activating the mordenite molecular sieve obtained in the step 1) at 400-600 ℃ in an inert atmosphere, then performing dealumination and silicon supplementation modification on the mordenite molecular sieve obtained in the step 1) by adopting a silicon tetrachloride isomorphous replacement method under a reaction condition, and purging after the reaction is finished;

3) and after purging, washing the molecular sieve with deionized water, performing ammonium ion exchange, and roasting at 400-600 ℃ in an air atmosphere for 3-10h to obtain the target molecular sieve.

As a specific embodiment, in step 1), the ion exchange method is prepared by the following steps:

(1) placing a mordenite sample in a soluble sodium salt solution with a certain concentration, wherein the liquid-solid ratio is 2-10 (weight ratio);

(2) stirring for 1-4 hours at 40-90 ℃;

(3) after solid-liquid separation, washing the mordenite sample by using deionized water until the solution is neutral;

(4) drying at 70-120 ℃, and then roasting at 450-600 ℃ for 2-6 hours to obtain the pretreated molecular sieve.

In one specific embodiment, the solution for sodium ion exchange is one of sodium nitrate, sodium chloride, sodium acetate, sodium carbonate and other sodium ion-containing solutions with a certain concentration.

As a specific implementation manner, in the step 2), a carrier gas is introduced into the reactor loaded with the molecular sieve for activation, then a mixed atmosphere carrying silicon tetrachloride saturated vapor is introduced for reaction and adsorption, the volume concentration of the silicon tetrachloride is 0-50%, and pure inert gas is switched to purge after adsorption saturation.

As a specific implementation manner, in the step 2), the inert atmosphere is one of nitrogen and helium or a mixed gas.

As a specific implementation manner, in the step 2), the reaction temperature of the silicon tetrachloride is 400-700 ℃, and the reaction time is 0.5-12 h.

As a specific embodiment, in step 2), after the isomorphous replacement reaction is completed, the residual silicon tetrachloride in the system is completely removed.

As a specific embodiment, in step 3), the molecular sieve should be washed clean of the solid products remaining in the molecular sieve with deionized water after the isomorphous metathesis reaction.

Examples 1 to 9

The mordenite molecular sieve catalyst with the silicon-aluminum ratio of 10 in the embodiment is modified by adopting the following steps:

1) uniformly mixing 5g of the sodium mordenite molecular sieve and 30ml of sodium nitrate aqueous solution with the molar concentration of 0.5mol/ml, uniformly stirring for 2 hours at 80 ℃, washing for three times by deionized water, drying for 12 hours at 120 ℃, and roasting for 6 hours at 500 ℃ to obtain the Na-MOR molecular sieve;

2) SiCl is carried out on sodium mordenite molecular sieve at reaction temperature by adopting chemical gas-solid phase reaction method₄Modification: 4g of Na-MOR molecular sieve is placed in a fixed bed quartz tube reactor, nitrogen is introduced at 500 ℃ for activation for 2h, and then the temperature is raised to 550 ℃. Then introducing mixed gas of silicon tetrachloride saturated steam and nitrogen, wherein the volume concentration of the silicon tetrachloride saturated steam in the mixed gas is 5%, starting the reaction, and obtaining the mordenite with different elimination degrees of the twelve-membered ring acid sites in different reaction times. In example 1 the reaction time was0.5h, 1h for example 2, 2h for example 3, 3h for example 4, 4h for example 5, 6h for example 6, 8h for example 7, 10h for example 8, and 12h for example 9. After the reaction is finished, pure nitrogen is switched to feed, purging is carried out for 5 hours, and impurities such as silicon tetrachloride and the like which are remained in the reaction tube and are not chemically adsorbed are purged completely.

And after purging is finished, washing the obtained molecular sieve sample with deionized water, performing ammonium ion exchange, drying at 100 ℃ for 12h in an air atmosphere, and roasting at 500 ℃ for 6h to obtain the modified mordenite molecular sieve.

Wherein the ammonium ion exchange is: 3g of the obtained molecular sieve sample and 20ml of ammonium nitrate aqueous solution with the molar concentration of 0.5mol/ml are uniformly mixed, stirred at a constant speed for 3 hours at 80 ℃, washed with deionized water for three times and repeated for three times.

Examples 10 to 12

The sodium mordenite molecular sieve is modified, and the specific condition parameters are shown in Table 3.

TABLE 3

The concentration of the soluble sodium salt in examples 10 to 12 was the same as in example 1, the reaction temperature and time for the isomorphous substitution were the same as in example 6, and the other conditions were the same as in example 1.

Example 13

In this example, the soluble sodium salt was sodium nitrate, and the concentration was 0.01mol/ml, and the other condition parameters were the same as in example 1.

Example 14

In this example, the soluble sodium salt was sodium chloride, the concentration was 1mol/ml, and other parameters were the same as in example 1.

Example 15

Characterization results for modified mordenite molecular sieves in the examples

The molecular size of pyridine is 0.57nm, while the size of the twelve-membered ring channel of the main channel of mordenite is 0.65nm multiplied by 0.70nm, and the size of the eight-membered ring channel of the side pocket is 0.34nm multiplied by 0.48 nm. Therefore, pyridine molecules cannot diffuse into the side pocket eight-membered ring channels of the mordenite molecular sieve and can only be adsorbed in the twelve-membered ring channels, and pyridine generates specific signals on an infrared spectrogram after being adsorbed on the molecular sieve, so that pyridine infrared is a good means for representing the number of the acid sites of the twelve-membered ring and the side pocket eight-membered ring of the mordenite molecular sieve. The characterization results are shown in Table 1.

The specific test method comprises the following steps: and (3) characterizing the acid content in the side pocket and the 12-membered ring channel of the mordenite by a pyridine in-situ vacuum device and an infrared spectrometer. Firstly, preparing 10mg of mordenite molecular sieve to be measured into sample pieces with the same mass, thickness and area, filling the sample pieces into a pyridine in-situ vacuum device, activating for 1h at 450 ℃ under a vacuum environment, cooling to 50 ℃, starting to adsorb pyridine, desorbing for 1h at 150 ℃, removing the physically adsorbed pyridine, measuring a spectrogram, and calculating according to the spectrogram to obtain the number of acid sites contained in a 12-membered ring channel and a side pocket in the mordenite.

The molecular size of the isopropyl benzene is 0.68nm, the isopropyl benzene cannot diffuse into eight-membered ring channels of side pockets of the mordenite molecular sieve, and only can react in twelve-membered ring channels, so that the isopropyl benzene is a probe reaction well representing the acid position in the twelve-membered ring channels of the mordenite molecular sieve. The specific test method comprises the following steps: filling 0.5g of molecular sieve to be evaluated with 40-60 meshes in a fixed bed reactor, activating for 1h at 500 ℃ under a nitrogen atmosphere, cooling to 280 ℃, and introducing isopropylbenzene (WHSV ═ 2 h)^-1) The reaction was started, and 5min after sampling analysis by gas chromatograph, the initial conversion was calculated.

As can be seen from figure 1, with the increase of the isomorphous replacement reaction time, the conversion rate of cumene cracking is gradually reduced, and finally, the reaction hardly occurs, which indicates that the acid sites in the twelve-membered ring channels of the mordenite molecular sieve can be eliminated by using a method of isomorphous replacement dealumination and silicon supplementation by silicon tetrachloride. As can be seen from Table 1, with the increase of the reaction time, the number of acid sites in the twelve-membered ring channel of the mordenite is reduced, and the influence on the acid sites of the eight-membered ring of the side pocket is increased, so that the excellent isomorphous replacement reaction time interval is between 3 and 8 hours.

The number of acid sites in each pore channel after isomorphous replacement modification of the mordenite molecular sieves of examples 1-9 is shown in table 1.

TABLE 1

The results of the acid site test and cumene cleavage test of examples 10 to 14 are similar to the above results, and show that the acid sites in the twelve-membered ring channels of the mordenite molecular sieve can be eliminated by isomorphous replacement of dealuminated silicon supplement with silicon tetrachloride.

Examples 16 to 22

The mordenite molecular sieve catalyst with the silicon-aluminum ratio of 10 in the embodiment is modified by adopting the following steps:

1) uniformly mixing 5g of the sodium mordenite molecular sieve and 30ml of a sodium nitrate solution with the molar concentration of 0.6mol/ml, uniformly stirring for 4 hours at a constant speed at 50 ℃, washing for three times by using deionized water, drying for 12 hours at 100 ℃, and then roasting for 6 hours at 500 ℃ to obtain the Na-MOR molecular sieve;

2) SiCl is carried out on sodium mordenite molecular sieve at reaction temperature by adopting chemical gas-solid phase reaction method₄Modification: placing 4g of Na-MOR molecular sieve in a fixed bed quartz tube reactor, introducing nitrogen at 500 ℃ for activation for 2h, and adjusting different temperatures to obtain the mordenite with different elimination degrees of the twelve-membered ring acid sites. In example 16, a mixed gas of saturated vapor of silicon tetrachloride and nitrogen was introduced at 400 ℃, in example 17, a mixed gas of saturated vapor of silicon tetrachloride and nitrogen was introduced at 450 ℃, in example 18, a mixed gas of saturated vapor of silicon tetrachloride and nitrogen was introduced at 500 ℃, in example 19, a mixed gas of saturated vapor of silicon tetrachloride and nitrogen was introduced at 550 ℃, in example 20, a mixed gas of saturated vapor of silicon tetrachloride and nitrogen was introduced at 600 ℃A mixed gas of saturated vapor of silicon tetrachloride and nitrogen was introduced at 650 ℃ in example 21, and a mixed gas of saturated vapor of silicon tetrachloride and nitrogen was introduced at 700 ℃ in example 22. The volume concentration of silicon tetrachloride saturated vapor in the mixed gas is 5%, pure nitrogen is switched to feed after the reaction is finished for 2 hours, purging is carried out for 5 hours, and impurities such as residual non-chemisorption silicon tetrachloride and the like in the reaction tube are purged completely.

And after purging is finished, washing the obtained molecular sieve sample with deionized water, performing ammonium ion exchange, drying at 100 ℃ for 12h in an air atmosphere, and roasting at 500 ℃ for 6h to obtain the modified mordenite molecular sieve.

Wherein the ammonium ion exchange is: 3g of the obtained molecular sieve sample and 20ml of ammonium nitrate aqueous solution with the molar concentration of 0.5mol/ml are uniformly mixed, stirred at a constant speed for 3 hours at 80 ℃, washed with deionized water for three times and repeated for three times.

Molecular sieve characterization results of the examples

See example 15 for test characterization methods.

As can be seen from FIG. 2, with the increase of the adsorption temperature, the conversion rate of cumene cracking is gradually reduced, and finally, almost no reaction occurs, which indicates that the acid sites in the twelve-membered ring channels of the mordenite molecular sieve can be eliminated by using a method of silicon tetrachloride isomorphous replacement for dealumination and silicon supplementation. As can be seen from Table 2, the modification effect is significant with the increase of the reaction temperature before 550 ℃, the influence on the side pocket acid site is small, the number of the twelve-membered ring acid sites is further reduced with the increase of the reaction temperature before 550 ℃, and the side pocket acid site is greatly influenced at the time.

The number of acid sites in each pore channel after isomorphous replacement modification of the mordenite molecular sieves of examples 16-22 is shown in table 2.

TABLE 2

	Sample name/Condition	Twelve membered ring acid site (mmol/g)	Side pocket acid site (mmol/g)
				HMOR	HMOR	0.216	0.286
Example 16	400℃	0.196	0.283
				Example 17	450℃	0.171	0.279
Example 18	500℃	0.121	0.267
				Example 19	550℃	0.051	0.238
Example 20	600℃	0.031	0.173
				Example 21	650℃	0.012	0.121
Example 22	700℃	0.005	0.085

Example 23

XRF analysis of Na-MOR prepared in examples 1 to 14 and 16 to 22 was carried out, and the cation in the sample was completely Na⁺。

Although the present application has been described with reference to a few embodiments, it should be understood that various changes, substitutions and alterations can be made herein without departing from the spirit and scope of the application as defined by the appended claims.