阅读说明：本技术 一种分子筛催化无机纤维及其制备方法和除尘脱硝一体化应用 (Molecular sieve catalytic inorganic fiber, preparation method thereof and dust removal and denitration integrated application ) 是由 陈运法 李伟曼 刘海弟 于 2021-07-06 设计创作，主要内容包括：本发明提供了一种分子筛催化无机纤维及其制备方法和除尘脱硝一体化应用,所述分子筛催化无机纤维的制备方法通过在无机纤维上原位生长离子交换型分子筛得到分子筛催化无机纤维,不仅具有较宽的脱硝温度窗口,还具有较强的耐水耐硫性能,而且由于催化组分在无机纤维上以Si-O-Si和Si-O-Al等化学键的方式牢固结合,不容易脱落,从而使得本发明所述分子筛催化无机纤维既可以与原始纤维混合,经压制成型处理得到除尘脱硝模块；又可以与原始纤维混纺,经针刺处理得到除尘脱硝模块,有助于实现非电行业烟气净化的除尘脱硝一体化应用。(The invention provides a molecular sieve catalytic inorganic fiber, a preparation method thereof and dust removal and denitration integrated application, wherein the preparation method of the molecular sieve catalytic inorganic fiber obtains the molecular sieve catalytic inorganic fiber by in-situ growing an ion exchange type molecular sieve on the inorganic fiber, so that the molecular sieve catalytic inorganic fiber not only has a wider denitration temperature window, but also has stronger water and sulfur resistance, and because catalytic components are firmly combined on the inorganic fiber in the mode of chemical bonds such as Si-O-Si, Si-O-Al and the like and are not easy to fall off, the molecular sieve catalytic inorganic fiber can be mixed with original fiber, and a dust removal and denitration module is obtained by compression molding treatment; and the dust removal and denitration module can be obtained by blending with the original fiber and needling treatment, and is beneficial to realizing the integrated application of dust removal and denitration in flue gas purification in the non-electric industry.)

1. A preparation method of inorganic fibers catalyzed by molecular sieves is characterized by comprising the following steps:

(1) pretreating inorganic fibers;

(2) preparing a molecular sieve precursor solution;

(3) immersing the inorganic fiber obtained by the pretreatment in the step (1) in the molecular sieve precursor solution in the step (2) for hydrothermal reaction, and sequentially carrying out solid-liquid separation, washing and drying to obtain a molecular sieve catalytic inorganic fiber crude product;

(4) immersing the molecular sieve catalytic inorganic fiber crude product in the step (3) in a metal salt solution for metal ion exchange, and sequentially carrying out solid-liquid separation and calcination to obtain the molecular sieve catalytic inorganic fiber;

wherein, the step (1) and the step (2) have no sequence;

alternatively, the preparation method comprises the following steps:

(1') pretreating inorganic fibers;

(2') preparing a metal ion type molecular sieve precursor solution;

(3 ') immersing the inorganic fiber obtained by the pretreatment in the step (1 ') in the metal ion type molecular sieve precursor solution in the step (2 ') to perform hydrothermal reaction, and sequentially performing solid-liquid separation, washing and drying to obtain the molecular sieve catalytic inorganic fiber;

wherein, the step (1 ') and the step (2') have no sequence.

2. The production method according to claim 1, wherein the inorganic fibers of step (1) or step (1') include any one of or a combination of at least two of aluminosilicate fibers, mullite fibers, or basalt fibers;

preferably, the pretreatment of step (1) or step (1') comprises washing and drying;

preferably, the washing comprises immersing the inorganic fibers in an organic solvent;

preferably, the organic solvent comprises ethanol and/or acetone;

preferably, the molecular sieve precursor solution in step (2) comprises a double ten-membered ring cross channel type molecular sieve precursor solution;

preferably, the molecular sieve precursor solution in step (2) comprises ethyl orthosilicate, sodium metaaluminate, tetrapropyl sodium hydroxide and deionized water;

preferably, in the molecular sieve precursor solution in the step (2), the molar ratio of the ethyl orthosilicate, the sodium metaaluminate, the tetrapropyl sodium hydroxide and the deionized water is (5-30):1, (5-10): 500-1000).

3. The preparation method according to claim 1 or 2, wherein the temperature of the hydrothermal reaction in step (3) is 100-140 ℃;

preferably, the hydrothermal reaction time of the step (3) is 24-48 h;

preferably, the hydrothermal reaction in the step (3) is carried out in a reaction kettle;

preferably, the metal salt in the metal salt solution of step (4) comprises any one of copper nitrate, manganese nitrate or iron nitrate or a combination of at least two of the above;

preferably, the concentration of the metal salt solution in the step (4) is 0.001-0.01 mol/L;

preferably, the temperature of the metal ion exchange in the step (4) is 60-100 ℃;

preferably, the time for the metal ion exchange in the step (4) is 8-12 h;

preferably, the temperature of the calcination in the step (4) is 500-550 ℃;

preferably, the calcination time of the step (4) is 4-8 h.

4. The preparation method of any one of claims 1 to 3, wherein before the metal ion exchange in step (4), the crude molecular sieve catalytic inorganic fibers in step (3) are immersed in an ammonium salt solution for hydrogen ion exchange, and then subjected to solid-liquid separation and calcination sequentially to obtain hydrogen ion exchanged molecular sieve catalytic inorganic fibers;

preferably, the ammonium salt in the ammonium salt solution comprises ammonium nitrate and/or ammonium chloride;

preferably, the concentration of the ammonium salt solution is 1-2 mol/L;

preferably, the temperature of the hydrogen ion exchange is 60-100 ℃;

preferably, the time for the hydrogen ion exchange is 8-12 h;

preferably, the temperature of the calcination is 500-550 ℃;

preferably, the calcination time is 4-8 h.

5. The process of any one of claims 1-4, wherein the metal ion type molecular sieve precursor solution of step (2') comprises a double ten-membered ring cross channel type molecular sieve precursor solution containing metal ions;

preferably, the precursor solution of the metal ion type molecular sieve in step (2') comprises ethyl orthosilicate, sodium metaaluminate, metal salt, tetrapropyl sodium hydroxide and deionized water;

preferably, in the precursor solution of the metal ionic molecular sieve in the step (2'), the molar ratio of the ethyl orthosilicate, the sodium metaaluminate, the metal salt, the tetrapropyl sodium hydroxide and the deionized water is (5-30):1, (0.005-0.01): (5-10): 500-);

preferably, the metal salt comprises any one of copper nitrate, manganese nitrate or iron nitrate or a combination of at least two thereof.

6. The method according to any one of claims 1 to 5, wherein the temperature of the hydrothermal reaction in step (3') is 100 ℃ to 140 ℃;

preferably, the hydrothermal reaction time of the step (3') is 24-48 h;

preferably, the hydrothermal reaction of step (3') is carried out in a reaction kettle.

7. The preparation method according to any one of claims 1 to 6, characterized in that the molecular sieve catalytic inorganic fiber obtained in step (3') is immersed in an ammonium salt solution for hydrogen ion exchange, and then subjected to solid-liquid separation and calcination in sequence to obtain hydrogen ion exchanged molecular sieve catalytic inorganic fiber;

preferably, the ammonium salt in the ammonium salt solution comprises ammonium nitrate and/or ammonium chloride;

preferably, the concentration of the ammonium salt solution is 1-2 mol/L;

preferably, the temperature of the hydrogen ion exchange is 60-100 ℃;

preferably, the time for the hydrogen ion exchange is 8-12 h;

preferably, the temperature of the calcination is 500-550 ℃;

preferably, the calcination time is 4-8 h.

8. The production method according to any one of claims 1 to 7, characterized by comprising the steps of:

(1) the method comprises the following steps of (1) pretreating inorganic fibers, wherein the pretreatment comprises the steps of cleaning and drying in sequence; the cleaning comprises immersing the inorganic fibers in ethanol and/or acetone;

(2) preparing a precursor solution of the double-ten-membered-ring cross channel type molecular sieve; in the molecular sieve precursor solution, the molar ratio of ethyl orthosilicate, sodium metaaluminate, tetrapropyl sodium hydroxide and deionized water is (5-30):1, (5-10): 500-;

(3) immersing the inorganic fiber obtained by the pretreatment in the step (1) in the molecular sieve precursor solution in the step (2), and carrying out hydrothermal reaction in a reaction kettle, wherein the temperature of the hydrothermal reaction is 100-140 ℃ and the time is 24-48 h; sequentially carrying out solid-liquid separation, washing and drying to obtain a molecular sieve catalytic inorganic fiber crude product;

(4) immersing the molecular sieve catalytic inorganic fiber crude product in the step (3) in an ammonium salt solution with the concentration of 1-2mol/L for hydrogen ion exchange at the temperature of 60-100 ℃ for 8-12h, and sequentially carrying out solid-liquid separation and calcination at the temperature of 500-550 ℃ for 4-8h to obtain the molecular sieve catalytic inorganic fiber with the hydrogen ion exchange; immersing the obtained molecular sieve catalytic inorganic fiber subjected to hydrogen ion exchange in a metal salt solution with the concentration of 0.001-0.01mol/L for metal ion exchange, wherein the temperature of the metal ion exchange is 60-100 ℃, the time is 8-12h, and sequentially carrying out solid-liquid separation and calcination, wherein the calcination temperature is 500-550 ℃, and the time is 4-8h, so as to obtain the molecular sieve catalytic inorganic fiber; the metal salt in the metal salt solution comprises any one or the combination of at least two of copper nitrate, manganese nitrate or ferric nitrate;

wherein, the step (1) and the step (2) have no sequence;

alternatively, the preparation method comprises the following steps:

(1') pretreating inorganic fibers, wherein the pretreatment comprises washing and drying which are sequentially carried out; the cleaning comprises immersing the inorganic fibers in ethanol and/or acetone;

(2') preparing a metal ion type molecular sieve precursor solution; in the precursor solution of the metal ion type molecular sieve, the molar ratio of ethyl orthosilicate, sodium metaaluminate, metal salt, tetrapropyl sodium hydroxide and deionized water is (5-30):1, (0.005-0.01): 5-10): 500-); the metal salt comprises any one or a combination of at least two of copper nitrate, manganese nitrate or iron nitrate;

(3 ') immersing the inorganic fiber obtained by the pretreatment in the step (1 ') in the metal ion type molecular sieve precursor solution in the step (2 '), performing hydrothermal reaction in a reaction kettle at the temperature of 100 ℃ for 24-48h, and sequentially performing solid-liquid separation, washing and drying to obtain the molecular sieve catalytic inorganic fiber;

(4 ') immersing the molecular sieve catalytic inorganic fiber obtained in the step (3') in an ammonium salt solution with the concentration of 1-2mol/L for hydrogen ion exchange at the temperature of 60-100 ℃ for 8-12h, and sequentially carrying out solid-liquid separation and calcination at the temperature of 500-550 ℃ for 4-8h to obtain the molecular sieve catalytic inorganic fiber with the hydrogen ion exchange;

wherein, the step (1 ') and the step (2') have no sequence.

9. A molecular sieve catalyzed inorganic fiber, obtained by the method of any one of claims 1 to 8.

10. The integrated dedusting and denitration application of the molecular sieve catalytic inorganic fiber is characterized in that the dedusting and denitration module is obtained by mixing the molecular sieve catalytic inorganic fiber of claim 9 with original fiber and then performing compression molding treatment, or the dedusting and denitration module is obtained by blending the molecular sieve catalytic inorganic fiber of claim 9 with the original fiber and then performing needling treatment.

Technical Field

The invention relates to the technical field of flue gas purification, in particular to a molecular sieve catalytic inorganic fiber, a preparation method thereof and dust removal and denitration integrated application.

Background

Nitrogen Oxides (NO)_X) Is an important atmospheric pollutant and can cause pollution such as haze, photochemical smog, acid rain and the like. At present, the fixed source emission of nitrogen oxides in China still occupies a large proportion, and NO in non-electric industry is still generated under the condition that most coal-fired power plants realize ultralow emission_XEmission control becomes one of the main hard links at the present stage. Ammonia selective catalytic reduction technology (NH)₃-selective catalytic reduction，NH₃SCR) is controlling NO_XThe main emission technologies are widely used in power plant boilers. On the one hand, however, the flue gas of the industrial boiler in the non-electric industry has complex components, often contains components such as sulfur dioxide, nitrogen oxide and particulate matters, and has the characteristics of low temperature window and the like, so that NH is greatly limited₃Rapid application of SCR technology in the industry. For example, in the cement industry, the coal-fired flue gas of a rotary kiln has the characteristics of high-dust and high-alkalinity substances, and high-efficiency NH similar to that of a power plant boiler is adopted₃SCR denitration technology is easy to cause problems of catalyst blockage, catalyst poisoning and the like. On the other hand, the existing treatment technology of the flue gas of the industrial boiler in the non-electric industry is to serially connect a single control module, and has the problems of long flow, large occupied area, high investment and operation cost and the like. For example, in the industries of steel, glass, waste incineration and the like, NO in flue gas_XSmoke dust, dioxin, toxic and harmful volatile organic compounds (OHAPs) and the like are respectively removed through a denitration reactor, a dust remover and other equipment, so that the pollutant removal system has the advantages of wide occupied area, large resistance, high energy consumption, high investment and the likeAnd the running cost is high, the burden of production enterprises is further increased, and the economical efficiency is poor. Therefore, the multi-component cooperative treatment and functional coupling technology is an effective way to solve the above problems, wherein the coupling of the gas treatment technology and the dust removal module is one of the research focuses thereof.

The existing dust removal and denitration coupling module can be divided into a low-temperature module represented by a catalytic filter bag and a medium-high temperature module represented by a catalytic ceramic membrane according to the tolerance temperature. The dust removal and denitration coupling module generally takes a dust removal module as a carrier and then loads a catalytic component. For example, CN108970269A discloses a composite filter bag for short-process dust removal and denitration of flue gas, wherein a plurality of catalyst coatings are coated on the inner surface of the filter bag substrate. CN108816220A discloses an electric-bag composite dust collector and a processing method thereof, wherein a precious metal is loaded on a filter bag of a bag-type dust collector by using a dipping method, and dust removal and denitration treatment are carried out when dust-containing flue gas passes through a module. However, in the dedusting and denitration module obtained by the methods, the binding force between the catalyst and the substrate is poor, and the catalytic component can fall off after the flue gas is washed for a long time, so that the service life of the filter bag is shortened.

In order to overcome the defect of loading catalytic components by soaking or coating, a plurality of researchers pay attention to the preparation of the composite catalytic filter material and prepare the composite filter bag by the traditional needling process. For example, CN112044177A is used for mixing low-temperature vanadium tungsten titanium powder with polytetrafluoroethylene powder, performing ball milling, extrusion, calendering and film cracking to prepare catalyst modified polytetrafluoroethylene fiber, blending with polytetrafluoroethylene chopped fiber, and weaving into filter bags by adopting a needling process. However, the synthesis method of the catalytic filter material is complex, the types of the catalysts are limited, and the large-scale popularization and use are not facilitated.

In recent years, with the fact that ion exchange type molecular sieve catalysts show good medium-low temperature denitration performance, researchers load the ion exchange type molecular sieve catalysts into a dedusting module to be applied to the field of flue gas purification in the non-electric industry, and the ion exchange type molecular sieve catalysts show good dedusting and denitration performance, but also have the problem that the catalysts are easy to fall off. In addition, inorganic fiber materials are often used for low-temperature modules represented by catalytic filter bags and medium-high temperature modules represented by catalytic ceramic membranes.

Therefore, the molecular sieve catalytic inorganic fiber and the preparation method thereof are developed, the molecular sieve is grown on the inorganic fiber in situ, the denitration catalyst has a wider denitration temperature window and stronger water-resistant and sulfur-resistant performances, and has the advantages that the catalytic component and the inorganic fiber are firmly combined and are not easy to fall off, and the dust removal and denitration integrated application can be realized in the field of flue gas purification in the non-electric industry.

Disclosure of Invention

In view of the problems in the prior art, the invention provides a molecular sieve catalytic inorganic fiber, a preparation method thereof and dust removal and denitration integrated application, the molecular sieve catalytic inorganic fiber obtained by in-situ growth of an ion exchange type molecular sieve on the inorganic fiber has a wider denitration temperature window and stronger water and sulfur resistance, and catalytic components are firmly combined on the inorganic fiber in the mode of chemical bonds such as Si-O-Si, Si-O-Al and the like and are not easy to fall off, so that the molecular sieve catalytic inorganic fiber can be mixed with original fibers and is subjected to compression molding to obtain a dust removal and denitration module; and the dust removal and denitration module can be obtained by blending with the original fiber through needling, and the dust removal and denitration integrated application of the flue gas purification in the non-electric industry is facilitated.

In order to achieve the purpose, the invention adopts the following technical scheme:

one of the purposes of the invention is to provide a preparation method of inorganic fiber catalyzed by molecular sieve, which comprises the following steps:

(1) pretreating inorganic fibers;

(2) preparing a molecular sieve precursor solution;

(3) immersing the inorganic fiber obtained by the pretreatment in the step (1) in the molecular sieve precursor solution in the step (2) for hydrothermal reaction, and sequentially carrying out solid-liquid separation, washing and drying to obtain a molecular sieve catalytic inorganic fiber crude product;

(4) immersing the molecular sieve catalytic inorganic fiber crude product in the step (3) in a metal salt solution for metal ion exchange, and sequentially carrying out solid-liquid separation and calcination to obtain the molecular sieve catalytic inorganic fiber;

wherein, the step (1) and the step (2) have no sequence;

alternatively, the preparation method comprises the following steps:

(1') pretreating inorganic fibers;

(2') preparing a metal ion type molecular sieve precursor solution;

(3 ') immersing the inorganic fiber obtained by the pretreatment in the step (1 ') in the metal ion type molecular sieve precursor solution in the step (2 ') to perform hydrothermal reaction, and sequentially performing solid-liquid separation, washing and drying to obtain the molecular sieve catalytic inorganic fiber;

wherein, the step (1 ') and the step (2') have no sequence.

According to the preparation method of the molecular sieve catalytic inorganic fiber, the molecular sieve catalytic inorganic fiber is obtained by growing the ion exchange type molecular sieve on the inorganic fiber in situ, so that the molecular sieve catalytic inorganic fiber not only has a wider denitration temperature window, but also has stronger water resistance and sulfur resistance, and because the catalytic components are firmly combined on the inorganic fiber in the mode of chemical bonds such as Si-O-Si, Si-O-Al and the like, and are not easy to fall off, the molecular sieve catalytic inorganic fiber can be mixed with the original fiber, and a dedusting and denitration module is obtained by compression molding treatment; and the dust removal and denitration module can be obtained by blending with the original fiber and needling treatment, and is beneficial to realizing the integrated application of dust removal and denitration in flue gas purification in the non-electric industry.

It is worth saying that in the hydrothermal reaction process of the present invention, the surface of the inorganic fiber is corroded by the highly alkaline molecular sieve precursor solution to release a trace amount of silicon source and aluminum source, and at the same time, the corroded rough surface is favorable for anchoring the silicon source and the aluminum source in the molecular sieve precursor solution to realize the directional growth of the molecular sieve crystal. Because the concentration of the silicon source and the aluminum source in the molecular sieve precursor solution is far higher than that of trace silicon source and aluminum source released by slight corrosion on the fiber surface, the growth speed of the molecular sieve crystal is also higher than the corrosion speed of the fibril, and a coaxial core-shell structure taking the fibril as an axis and the molecular sieve as a shell is finally formed.

In addition, the catalytic component on the molecular sieve catalytic inorganic fiber is an ion exchange type molecular sieve, namely, sodium ions in the molecular sieve realize metal ion exchange, and the prior art generally adopts a method of firstly obtaining the molecular sieve and then carrying out metal ion exchange, so that the metal ion exchange cannot be realized while the molecular sieve is generated. However, through many experimental studies, the inventor particularly prefers copper ions, iron ions, manganese ions and the like, under the condition of controlling the concentration of metal ions, the precursor sol can be disturbed as little as possible, metal salt required by metal ion exchange can be directly added into the molecular sieve precursor solution, and then the metal ion exchange can be realized while the molecular sieve is generated through hydrothermal reaction, so that the molecular sieve catalytic inorganic fiber meeting the requirements can be directly obtained. The method for realizing metal ion exchange while generating the molecular sieve through hydrothermal reaction can not only save the step of ion exchange of a single metal salt solution, shorten the synthesis flow, but also be beneficial to the greening of the synthesis process. Furthermore, by adjusting the ion species of the metal ion exchange, specific NH can be realized₃-adjustment of the catalytic performance of the SCR.

As a preferred technical scheme of the invention, the inorganic fibers in the step (1) or the step (1') comprise any one or a combination of at least two of aluminum silicate fibers, mullite fibers or basalt fibers, and typical but non-limiting examples of the combination are as follows: a combination of alumina silicate fibers and mullite fibers, a combination of mullite fibers and basalt fibers, a combination of alumina silicate fibers and basalt fibers, or the like.

Preferably, the pretreatment of step (1) or step (1') comprises washing and drying.

Preferably, the cleaning includes immersing the inorganic fibers in an organic solvent, which is effective not only in removing oil stains from the inorganic fibers but also in removing high-density impurities in the form of beads mixed in the inorganic fibers.

Preferably, the organic solvent comprises ethanol and/or acetone.

Preferably, the molecular sieve precursor solution in step (2) includes a double ten-membered ring cross channel type molecular sieve precursor solution, i.e., an MFI type molecular sieve precursor solution.

Preferably, the molecular sieve precursor solution in step (2) includes ethyl orthosilicate, sodium metaaluminate, tetrapropyl sodium hydroxide and deionized water, i.e., a molecular sieve precursor solution corresponding to the ZSM-5 type molecular sieve.

Preferably, in the molecular sieve precursor solution in the step (2), the molar ratio of the ethyl orthosilicate, the sodium metaaluminate, the tetrapropylsodium hydroxide and the deionized water is (5-30):1 (5-10): 500-1000, such as 5:1:5:500, 5:1:5:800, 5:1:5:1000, 5:1:7:500, 5:1:7:800, 5:1:7:1000, 5:1:10:500, 5:1:10:800, 5:1:10:1000, 10:1:5:500, 10:1:5:1000, 10:1:10:500, 10:1:10:1000, 30:1:5:500, 30:1:5:1000, 30:1:10:500 or 30:1:10:1000, but the values are not limited to the enumerated values, and other values not enumerated in the range are also applicable.

As a preferred embodiment of the present invention, the temperature of the hydrothermal reaction in the step (3) is 100-140 ℃, for example, 100 ℃, 105 ℃, 110 ℃, 115 ℃, 120 ℃, 125 ℃, 130 ℃, 135 ℃ or 140 ℃, but is not limited to the recited values, and other values not recited in the range of the values are also applicable.

Preferably, the hydrothermal reaction time in step (3) is 24-48h, such as 24h, 28h, 32h, 36h, 40h, 42h, 44h or 48h, but not limited to the recited values, and other values not recited in the range of the recited values are also applicable.

Preferably, the hydrothermal reaction in step (3) is carried out in a reaction kettle.

Preferably, the metal salt in the metal salt solution of step (4) comprises any one of copper nitrate, manganese nitrate or iron nitrate or a combination of at least two of them, typical but non-limiting examples of which are: a combination of copper nitrate and manganese nitrate, a combination of manganese nitrate and iron nitrate, or a combination of copper nitrate and iron nitrate, or the like.

Preferably, the metal salt solution in step (4) has a concentration of 0.001-0.01mol/L, such as 0.001mol/L, 0.002mol/L, 0.003mol/L, 0.005mol/L, 0.006mol/L, 0.007mol/L, 0.009mol/L, or 0.01mol/L, but not limited to the recited values, and other values not recited in the range of values are equally applicable.

Preferably, the temperature of the metal ion exchange in step (4) is 60 to 100 ℃, such as 60 ℃, 65 ℃, 70 ℃, 75 ℃, 80 ℃, 85 ℃, 90 ℃, 95 ℃ or 100 ℃, but not limited to the recited values, and other values not recited in the range of values are also applicable.

Preferably, the metal ion exchange time in step (4) is 8-12h, such as 8h, 8.5h, 9h, 9.5h, 10h, 10.5h, 11h, 11.5h or 12h, but not limited to the recited values, and other values not recited in the range of the values are also applicable.

Preferably, the temperature of the calcination in step (4) is 500-550 ℃, such as 500 ℃, 505 ℃, 510 ℃, 515 ℃, 520 ℃, 525 ℃, 530 ℃, 535 ℃, 540 ℃, 545 ℃ or 550 ℃, but not limited to the recited values, and other unrecited values within the range of the values are also applicable.

Preferably, the calcination in step (4) is carried out for 4-8h, such as 4h, 4.5h, 5h, 5.5h, 6h, 6.5h, 7h, 7.5h or 8h, but not limited to the recited values, and other values not recited in the range of the values are also applicable.

As a preferable technical scheme of the invention, before the metal ion exchange in the step (4), the molecular sieve catalytic inorganic fiber crude product in the step (3) is immersed in an ammonium salt solution for hydrogen ion exchange, and the hydrogen ion exchanged molecular sieve catalytic inorganic fiber is obtained through solid-liquid separation and calcination in sequence.

It is worth to be noted that, in the step (4) of the present invention, hydrogen ion exchange is performed first to make the molecular sieve have sufficient acidic sites, and then metal ion exchange is performed to facilitate a portion of metal ions to exchange into the molecular sieve framework, so that the catalytic performance of the molecular sieve can be effectively improved through the mutual synergistic effect of hydrogen ion exchange and metal ion exchange.

Preferably, the ammonium salt in the ammonium salt solution comprises ammonium nitrate and/or ammonium chloride.

Preferably, the ammonium salt solution has a concentration of 1 to 2mol/L, such as 1mol/L, 1.1mol/L, 1.2mol/L, 1.3mol/L, 1.4mol/L, 1.5mol/L, 1.6mol/L, 1.7mol/L, 1.8mol/L, 1.9mol/L, or 2mol/L, and the like, but is not limited to the recited values, and other values not recited in the range of values are equally applicable.

Preferably, the temperature of the hydrogen ion exchange is 60 to 100 ℃, such as 60 ℃, 65 ℃, 70 ℃, 75 ℃, 80 ℃, 85 ℃, 90 ℃, 95 ℃ or 100 ℃, but is not limited to the recited values, and other values not recited within the range of values are equally applicable.

Preferably, the hydrogen ion exchange time is 8 to 12 hours, such as 8 hours, 8.5 hours, 9 hours, 9.5 hours, 10 hours, 10.5 hours, 11 hours, 11.5 hours, or 12 hours, but not limited to the recited values, and other values not recited within the range of values are equally applicable.

Preferably, the temperature of the calcination is 500-550 ℃, such as 500 ℃, 505 ℃, 510 ℃, 515 ℃, 520 ℃, 525 ℃, 530 ℃, 535 ℃, 540 ℃, 545 ℃ or 550 ℃, but is not limited to the recited values, and other values not recited in the range of values are equally applicable.

Preferably, the calcination is carried out for a period of time of 4 to 8 hours, for example 4 hours, 4.5 hours, 5 hours, 5.5 hours, 6 hours, 6.5 hours, 7 hours, 7.5 hours or 8 hours, etc., but not limited to the recited values, and other values not recited within the range of values are also applicable.

As a preferred technical scheme of the invention, the metal ion type molecular sieve precursor solution in the step (2') comprises a double ten-membered ring cross channel type molecular sieve precursor solution containing metal ions.

Preferably, the precursor solution of the metal ion type molecular sieve in step (2') comprises ethyl orthosilicate, sodium metaaluminate, metal salt, tetrapropyl sodium hydroxide and deionized water.

Preferably, in the metal ionic molecular sieve precursor solution in the step (2'), the molar ratio of the ethyl orthosilicate, the sodium metaaluminate, the metal salt, the tetrapropylsodium hydroxide to the deionized water is (5-30):1 (0.005-0.01): 5-10) (500-1000), such as 5:1:0.005:5:500, 5:1:0.005:5:1000, 5:1:0.005:10:500, 5:1:0.005:10:1000, 5:1:0.01:5:500, 5:1:0.01:5:1000, 5:1:0.01:10:500, 5:1:0.01:10:1000, 30:1:0.005:5:500, 30:1:0.005:5:1000, 30:1:0.005: 500, 30:1:0.005:10:1000, 30:1:0.01: 0:500, 30:1:0.01: 0:1:10:1000, 30: 0.01: 500: 1:10:500, 30:1:10:1000, 30:1:0.01:10:500, 30: 10:1000, or 500, but not limited to, the recited values and other values not recited within the range of values are equally applicable.

Preferably, the metal salt comprises any one of copper nitrate, manganese nitrate or iron nitrate or a combination of at least two of these, typical but non-limiting examples being: a combination of copper nitrate and manganese nitrate, a combination of manganese nitrate and iron nitrate, or a combination of copper nitrate and iron nitrate, or the like.

As a preferred embodiment of the present invention, the temperature of the hydrothermal reaction in the step (3') is 100-140 ℃, for example, 100 ℃, 105 ℃, 110 ℃, 115 ℃, 120 ℃, 125 ℃, 130 ℃, 135 ℃ or 140 ℃, but is not limited to the values listed, and other values not listed in the range of the values are also applicable.

Preferably, the hydrothermal reaction time in step (3') is 24-48h, such as 24h, 28h, 32h, 36h, 40h, 42h, 44h or 48h, but not limited to the recited values, and other values not recited in the range of the recited values are also applicable.

Preferably, the hydrothermal reaction of step (3') is carried out in a reaction kettle.

And (3) immersing the molecular sieve catalytic inorganic fiber obtained in the step (3') in an ammonium salt solution for hydrogen ion exchange, and sequentially carrying out solid-liquid separation and calcination to obtain the hydrogen ion exchanged molecular sieve catalytic inorganic fiber.

It is worth to be noted that, after the step (3') of the present invention, hydrogen ion exchange is further performed, so that the hydrogen ion exchange and metal ion exchange realize a synergistic effect, and the catalytic performance of the molecular sieve can be effectively improved.

Preferably, the ammonium salt in the ammonium salt solution comprises ammonium nitrate and/or ammonium chloride.

Preferably, the ammonium salt solution has a concentration of 1 to 2mol/L, such as 1mol/L, 1.1mol/L, 1.2mol/L, 1.3mol/L, 1.4mol/L, 1.5mol/L, 1.6mol/L, 1.7mol/L, 1.8mol/L, 1.9mol/L, or 2mol/L, and the like, but is not limited to the recited values, and other values not recited in the range of values are equally applicable.

Preferably, the temperature of the hydrogen ion exchange is 60 to 100 ℃, such as 60 ℃, 65 ℃, 70 ℃, 75 ℃, 80 ℃, 85 ℃, 90 ℃, 95 ℃ or 100 ℃, but is not limited to the recited values, and other values not recited within the range of values are equally applicable.

Preferably, the hydrogen ion exchange time is 8 to 12 hours, such as 8 hours, 8.5 hours, 9 hours, 9.5 hours, 10 hours, 10.5 hours, 11 hours, 11.5 hours, or 12 hours, but not limited to the recited values, and other values not recited within the range of values are equally applicable.

Preferably, the temperature of the calcination is 500-550 ℃, such as 500 ℃, 505 ℃, 510 ℃, 515 ℃, 520 ℃, 525 ℃, 530 ℃, 535 ℃, 540 ℃, 545 ℃ or 550 ℃, but is not limited to the recited values, and other values not recited in the range of values are equally applicable.

Preferably, the calcination is carried out for a period of time of 4 to 8 hours, for example 4 hours, 4.5 hours, 5 hours, 5.5 hours, 6 hours, 6.5 hours, 7 hours, 7.5 hours or 8 hours, etc., but not limited to the recited values, and other values not recited within the range of values are also applicable.

As a preferred technical scheme of the invention, the preparation method comprises the following steps:

(1) the method comprises the following steps of (1) pretreating inorganic fibers, wherein the pretreatment comprises the steps of cleaning and drying in sequence; the cleaning comprises immersing the inorganic fibers in ethanol and/or acetone;

(2) preparing a precursor solution of the double-ten-membered-ring cross channel type molecular sieve; in the molecular sieve precursor solution, the molar ratio of ethyl orthosilicate, sodium metaaluminate, tetrapropyl sodium hydroxide and deionized water is (5-30):1, (5-10): 500-;

(3) immersing the inorganic fiber obtained by the pretreatment in the step (1) in the molecular sieve precursor solution in the step (2), and carrying out hydrothermal reaction in a reaction kettle, wherein the temperature of the hydrothermal reaction is 100-140 ℃ and the time is 24-48 h; sequentially carrying out solid-liquid separation, washing and drying to obtain a molecular sieve catalytic inorganic fiber crude product;

(4) immersing the molecular sieve catalytic inorganic fiber crude product in the step (3) in an ammonium salt solution with the concentration of 1-2mol/L for hydrogen ion exchange at the temperature of 60-100 ℃ for 8-12h, and sequentially carrying out solid-liquid separation and calcination at the temperature of 500-550 ℃ for 4-8h to obtain the molecular sieve catalytic inorganic fiber with the hydrogen ion exchange; immersing the obtained molecular sieve catalytic inorganic fiber subjected to hydrogen ion exchange in a metal salt solution with the concentration of 0.001-0.01mol/L for metal ion exchange, wherein the temperature of the metal ion exchange is 60-100 ℃, the time is 8-12h, and sequentially carrying out solid-liquid separation and calcination, wherein the calcination temperature is 500-550 ℃, and the time is 4-8h, so as to obtain the molecular sieve catalytic inorganic fiber; the metal salt in the metal salt solution comprises any one or the combination of at least two of copper nitrate, manganese nitrate or ferric nitrate;

wherein, the step (1) and the step (2) have no sequence;

alternatively, the preparation method comprises the following steps:

(1') pretreating inorganic fibers, wherein the pretreatment comprises washing and drying which are sequentially carried out; the cleaning comprises immersing the inorganic fibers in ethanol and/or acetone;

(2') preparing a metal ion type molecular sieve precursor solution; in the precursor solution of the metal ion type molecular sieve, the molar ratio of ethyl orthosilicate, sodium metaaluminate, metal salt, tetrapropyl sodium hydroxide and deionized water is (5-30):1, (0.005-0.01): 5-10): 500-); the metal salt comprises any one or a combination of at least two of copper nitrate, manganese nitrate or iron nitrate;

(3 ') immersing the inorganic fiber obtained by the pretreatment in the step (1 ') in the metal ion type molecular sieve precursor solution in the step (2 '), performing hydrothermal reaction in a reaction kettle at the temperature of 100 ℃ for 24-48h, and sequentially performing solid-liquid separation, washing and drying to obtain the molecular sieve catalytic inorganic fiber;

(4 ') immersing the molecular sieve catalytic inorganic fiber obtained in the step (3') in an ammonium salt solution with the concentration of 1-2mol/L for hydrogen ion exchange at the temperature of 60-100 ℃ for 8-12h, and sequentially carrying out solid-liquid separation and calcination at the temperature of 500-550 ℃ for 4-8h to obtain the molecular sieve catalytic inorganic fiber with the hydrogen ion exchange;

wherein, the step (1 ') and the step (2') have no sequence.

The second purpose of the invention is to provide a molecular sieve catalytic inorganic fiber which is obtained by the preparation method of the first purpose.

The invention also aims to provide a dust removal and denitration integrated application of the molecular sieve catalytic inorganic fiber, wherein the dust removal and denitration module is obtained by mixing the molecular sieve catalytic inorganic fiber of the second aim with the original fiber and performing compression molding treatment, for example, the dust removal and denitration module is obtained by mixing the molecular sieve catalytic inorganic fiber with the original fiber, adding a proper amount of binder, performing compression molding and low-temperature calcination to obtain a rigid catalytic ceramic membrane body.

It is worth to say that, the dedusting and denitration module is directly formed by stacking fibers, can be directly molded by applying pressure (5-10MPa) based on the principle of contact hardening, and does not add pore-forming agents, so that a hard catalytic ceramic membrane body can be obtained without high-temperature calcination; furthermore, the inventors believe that high temperature calcination adversely affects the performance of the molecular sieve catalytic inorganic fibers.

Or, after the second-purpose molecular sieve catalytic inorganic fiber is blended with the original fiber, the dust-removing and denitration module is obtained through needling, for example, the flexible filter bag is obtained through processes such as needling.

Compared with the prior art, the invention at least has the following beneficial effects:

(1) according to the preparation method of the molecular sieve catalytic inorganic fiber, the molecular sieve catalytic inorganic fiber is obtained by growing the ion exchange type molecular sieve on the inorganic fiber in situ, so that the catalytic inorganic fiber not only has a wider denitration temperature window, but also has stronger water resistance and sulfur resistance, and because the catalytic component is firmly combined on the inorganic fiber in a chemical bond mode of Si-O-Si or Si-O-Al and the like and is not easy to fall off, the molecular sieve catalytic inorganic fiber not only can be mixed with the original fiber and then subjected to compression molding treatment to obtain the dust removal and denitration module, but also can be blended with the original fiber and then subjected to needling treatment to obtain the dust removal and denitration module, and the dust removal and denitration integrated application of non-electric industry flue gas purification is facilitated;

(2) according to the preparation method of the molecular sieve catalytic inorganic fiber, the metal salt required by metal ion exchange can be directly added into the molecular sieve precursor solution, so that the metal ion exchange can be realized while the molecular sieve is generated through hydrothermal reaction, the molecular sieve catalytic inorganic fiber meeting the requirements can be directly obtained, the step of separate metal salt solution ion exchange can be omitted, the synthesis process is shortened, and the synthesis process is beneficial to greenization.

Drawings

FIG. 1 is a scanning electron microscope image of the molecular sieve catalytic inorganic fiber prepared in example 1 of the present invention;

FIG. 2 is an XRD pattern of the molecular sieve catalytic inorganic fiber prepared in example 1 of the present invention;

FIG. 3 is a scanning electron microscope image of the molecular sieve catalytic inorganic fiber prepared in example 2 of the present invention;

FIG. 4 is an XRD pattern of the molecular sieve catalytic inorganic fiber prepared in example 2 of the present invention.

Detailed Description

The technical scheme of the invention is further explained by the specific implementation mode in combination with the attached drawings.

To better illustrate the invention and to facilitate the understanding of the technical solutions thereof, typical but non-limiting examples of the invention are as follows:

unless otherwise specified, the following examples used chemicals and materials that were sourced from common chemical stores without further purification and optimization.

Example 1

The embodiment provides a preparation method of inorganic fibers catalyzed by molecular sieves, which comprises the following steps:

(1) pretreating inorganic fibers:

soaking a certain amount of aluminum silicate fiber with ethanol, not only effectively removing oil stains on the inorganic fiber, but also allowing high-density impurities in the shape of a ball mixed in the inorganic fiber to sink to the bottom for removing, and then simply washing with ethanol, and drying in an oven at 80 ℃ for overnight;

(2) preparing MFI type molecular sieve precursor solution:

respectively weighing the components according to the molar ratio of tetraethoxysilane, sodium metaaluminate, tetrapropyl sodium hydroxide and deionized water of 25:1:5:1000, and mixing to obtain an MFI type molecular sieve precursor solution;

(3) hydrothermal synthesis of inorganic fiber catalyzed by molecular sieve:

immersing the aluminum silicate fiber obtained by the pretreatment in the step (1) in the molecular sieve precursor solution in the step (2), and carrying out hydrothermal reaction in a reaction kettle, wherein the temperature of the hydrothermal reaction is 140 ℃ and the time is 24 hours; sequentially carrying out solid-liquid separation, washing and drying to obtain a molecular sieve catalytic inorganic fiber crude product;

(4) the molecular sieve catalyzes the ion exchange of the inorganic fibers:

immersing the molecular sieve catalytic inorganic fiber crude product in the step (3) in NH with the concentration of 1mol/L₄NO₃Performing hydrogen ion exchange in the solution, performing ion exchange for 10 hours under the condition of 80 ℃ water bath, and sequentially performing solid-liquid separation and calcination at 550 ℃ for 4 hours to obtain hydrogen ion exchanged molecular sieve catalytic inorganic fiber; immersing the obtained hydrogen ion exchanged molecular sieve catalytic inorganic fiber in a copper nitrate solution with the concentration of 0.005mol/L for metal ion exchange, carrying out ion exchange for 10 hours under the condition of 80 ℃ water bath, and sequentially carrying out solid-liquid separation and calcination at the temperature of 550 ℃ for 4 hours to obtain the molecular sieve catalytic inorganic fiber;

wherein, the step (1) and the step (2) have no sequence.

The scanning electron microscope image of the molecular sieve catalytic inorganic fiber prepared in this example is shown in fig. 1, and the XRD image is shown in fig. 2. It can be seen from fig. 1 that the molecular sieve grows in situ on the inorganic fiber to form a coaxial core-shell structure with the inorganic fiber as the axis and the molecular sieve as the shell.

Example 2

The embodiment provides a preparation method of inorganic fibers catalyzed by molecular sieves, which comprises the following steps:

(1') pretreating inorganic fibers:

soaking a certain amount of basalt fibers with ethanol, not only effectively removing oil stains on the inorganic fibers, but also allowing high-density impurities in the form of beads mixed in the inorganic fibers to sink to the bottom for removing, and then simply washing with ethanol, and drying in an oven at 80 ℃ for overnight;

(2') preparing a metal ionic molecular sieve precursor solution:

respectively weighing the components according to the molar ratio of tetraethoxysilane to sodium metaaluminate to copper nitrate to tetrapropyl sodium hydroxide to deionized water of 25:1:0.005:5:1000, and mixing the components to obtain a precursor solution of the metal ion type molecular sieve;

(3') hydrothermal synthesis of inorganic fibers catalyzed by molecular sieves:

immersing the basalt fiber obtained by the pretreatment in the step (1 ') in the metal ion type molecular sieve precursor solution in the step (2'), performing hydrothermal reaction in a reaction kettle at the temperature of 140 ℃ for 24 hours, and sequentially performing solid-liquid separation, washing and drying to obtain the molecular sieve catalytic inorganic fiber;

(4') molecular sieves catalyze hydrogen ion exchange of inorganic fibers:

immersing the molecular sieve catalytic inorganic fiber obtained in the step (3') in 1mol/L NH₄NO₃Performing hydrogen ion exchange in the solution, performing ion exchange for 10 hours under the condition of 80 ℃ water bath, and sequentially performing solid-liquid separation and calcination at 550 ℃ for 4 hours to obtain hydrogen ion exchanged molecular sieve catalytic inorganic fiber;

wherein, the step (1 ') and the step (2') have no sequence.

The scanning electron microscope image of the molecular sieve catalytic inorganic fiber prepared in this example is shown in fig. 3, and the XRD image is shown in fig. 4. It can be seen from fig. 3 that the molecular sieve grows in situ on the inorganic fiber to form a coaxial core-shell structure with the inorganic fiber as the axis and the molecular sieve as the shell.

It should be noted that since the alumina silicate fiber in example 1 is amorphous and the basalt fiber in example 2 is amorphous, only the peaks of the ion exchange type molecular sieve are observed in the XRD patterns corresponding to example 1 and example 2, and both peaks are identical.

Example 3

The embodiment provides a preparation method of inorganic fibers catalyzed by molecular sieves, which comprises the following steps:

(1') pretreating inorganic fibers:

immersing a certain amount of mullite fiber by using ethanol, not only effectively removing oil stains on the inorganic fiber, but also allowing high-density impurities in a bead shape mixed in the inorganic fiber to sink to the bottom for removing, and then simply washing by using ethanol, and drying in an oven at 80 ℃ for overnight;

(2') preparing a metal ionic molecular sieve precursor solution:

respectively weighing the components according to the molar ratio of ethyl orthosilicate to sodium metaaluminate to copper nitrate to tetrapropyl sodium hydroxide to deionized water of 5:1:0.005:5:500, and mixing the components to obtain a precursor solution of the metal ion type molecular sieve;

(3') hydrothermal synthesis of inorganic fibers catalyzed by molecular sieves:

immersing the mullite fiber obtained by the pretreatment in the step (1 ') in the metal ion type molecular sieve precursor solution in the step (2'), carrying out hydrothermal reaction in a reaction kettle at the temperature of 100 ℃ for 48 hours, and sequentially carrying out solid-liquid separation, washing and drying to obtain the molecular sieve catalytic inorganic fiber;

(4') molecular sieves catalyze hydrogen ion exchange of inorganic fibers:

immersing the molecular sieve catalytic inorganic fiber obtained in the step (3') in NH with the concentration of 1mol/L₄Carrying out hydrogen ion exchange in a Cl solution, carrying out ion exchange for 12 hours under the condition of water bath at the temperature of 60 ℃, and sequentially carrying out solid-liquid separation and calcination at the temperature of 500 ℃ for 8 hours to obtain the molecular sieve catalytic inorganic fiber for hydrogen ion exchange;

wherein, the step (1 ') and the step (2') have no sequence.

Example 4

The embodiment provides a preparation method of inorganic fibers catalyzed by molecular sieves, which comprises the following steps:

(1') pretreating inorganic fibers:

soaking a certain amount of basalt fibers with ethanol, not only effectively removing oil stains on the inorganic fibers, but also allowing high-density impurities in the form of beads mixed in the inorganic fibers to sink to the bottom for removing, and then simply washing with ethanol, and drying in an oven at 80 ℃ for overnight;

(2') preparing a metal ionic molecular sieve precursor solution:

respectively weighing the components according to the molar ratio of tetraethoxysilane to sodium metaaluminate to copper nitrate to tetrapropyl sodium hydroxide to deionized water of 30:1:0.01:10:1000, and mixing the components to obtain a precursor solution of the metal ion type molecular sieve;

(3') hydrothermal synthesis of inorganic fibers catalyzed by molecular sieves:

immersing the basalt fiber obtained by the pretreatment in the step (1 ') in the metal ion type molecular sieve precursor solution in the step (2'), carrying out hydrothermal reaction in a reaction kettle at the temperature of 120 ℃ for 36h, and sequentially carrying out solid-liquid separation, washing and drying to obtain the molecular sieve catalytic inorganic fiber;

(4') molecular sieves catalyze hydrogen ion exchange of inorganic fibers:

immersing the molecular sieve catalytic inorganic fiber obtained in the step (3') in 1mol/L NH₄NO₃Performing hydrogen ion exchange in the solution, performing ion exchange for 8h under the condition of 100 ℃ water bath, and sequentially performing solid-liquid separationCalcining at 520 ℃ for 6 hours to obtain the molecular sieve catalytic inorganic fiber with hydrogen ion exchange;

wherein, the step (1 ') and the step (2') have no sequence.

Application example 1

After the molecular sieve catalytic inorganic fiber prepared in the embodiment 1 is mixed with original fiber (aluminum silicate fiber), a proper amount of binder is added, and the mixture is subjected to press forming and low-temperature calcination, so that a rigid catalytic ceramic membrane body serving as a dedusting and denitration module can be obtained, and the dedusting and denitration integrated application of flue gas purification in the non-electric industry is realized.

Application example 2

After the molecular sieve catalytic inorganic fiber prepared in example 2 is mixed with the original fiber (basalt fiber), a proper amount of binder is added, and the mixture is subjected to press forming and low-temperature calcination, so that a rigid catalytic ceramic membrane body serving as a dedusting and denitration module can be obtained, and the dedusting and denitration integrated application of flue gas purification in the non-electric industry is realized.

Example 3

After the molecular sieve catalytic inorganic fiber prepared in the embodiment 1 is mixed with the original fiber (aluminum silicate fiber) and the PVDF fiber, a proper amount of binder is added through blending, and the flexible filtering filter bag serving as a dedusting and denitration module is obtained through needling treatment, so that the dedusting and denitration integrated application of the flue gas purification in the non-electric industry is realized.

Application example 4

Mixing the molecular sieve catalytic inorganic fiber prepared in the example 2 with original fiber (basalt fiber), placing the mixture in a reaction kettle containing a small amount of water at 100 ℃, carrying out hydrothermal reaction for 10 hours, taking out the mixture, drying the mixture, placing the dried mixture in a mold, and applying pressure under the pressure of 5MPa to obtain the contact-hardened dedusting and denitration module.

Comparative example 1

This comparative example provides a method of preparing a molecular sieve catalyzed inorganic fiber, comprising the steps of:

(i) preparing molecular sieve powder:

respectively weighing the components according to the molar ratio of tetraethoxysilane, sodium metaaluminate, tetrapropyl sodium hydroxide and deionized water of 25:1:5:1000, and mixing to obtain an MFI type molecular sieve precursor solution; carrying out hydrothermal reaction on the obtained MFI type molecular sieve precursor solution in a reaction kettle, wherein the temperature of the hydrothermal reaction is 140 ℃, the time is 48 hours, and carrying out solid-liquid separation, water washing and ethanol washing in sequence to obtain a white solid;

the resulting white solid was immersed in 1mol/L NH₄NO₃Performing hydrogen ion exchange in the solution, performing ion exchange for 10 hours under the condition of 80 ℃ water bath, and sequentially performing solid-liquid separation and calcination at 550 ℃ for 4 hours to obtain a hydrogen ion exchanged molecular sieve; immersing the obtained hydrogen ion exchanged molecular sieve in a copper nitrate solution for metal ion exchange, carrying out ion exchange for 10 hours under the condition of 80 ℃ water bath, and sequentially carrying out solid-liquid separation and calcination at the temperature of 550 ℃ for 4 hours to obtain MFI type molecular sieve powder for Cu ion exchange;

(ii) mixing molecular sieve powder with inorganic fiber:

and (3) grinding the MFI type molecular sieve powder subjected to Cu ion exchange obtained in the step (i), mixing with aluminum silicate fibers, adding silica gel serving as a binder, pouring the uniformly mixed whole into a mold, and calcining at the low temperature of 500 ℃ for 4 hours to obtain the monolithic catalyst, wherein the mass ratio of the mixture of the MFI type molecular sieve powder to the aluminum silicate fibers is 1:100: 0.5.

And (3) performance characterization:

(1) binding force

Respectively weighing 1g of the molecular sieve catalytic inorganic fibers prepared in the embodiments 1 and 2, respectively putting the weighed 1g of the molecular sieve catalytic inorganic fibers into 50mL of deionized water, performing ultrasonic treatment for 10 minutes, and sequentially performing filtering, drying and weighing, wherein the weight loss rate of the molecular sieve catalytic inorganic fibers prepared in the embodiments 1 and 2 is only 2-5%, which indicates that the molecular sieve can be firmly combined on the inorganic fibers by the preparation method disclosed by the invention;

(2) catalytic temperature window capable of achieving denitration effect of more than 90%

The molecular sieve catalytic inorganic fiber prepared in the embodiment 1 can achieve NO removal efficiency of more than 90% at the temperature of 180-350 ℃; under the same experimental conditions, the molecular sieve catalytic inorganic fiber prepared in example 2 can achieve NO removal efficiency of more than 90% within 360 ℃ of 120-;

the molecular sieve catalytic inorganic fiber prepared in the embodiment 2 can achieve NO removal efficiency of more than 90% at the temperature of 120-360 ℃; under the same experimental conditions, the mixture of the molecular sieve powder and the aluminum silicate fiber (before the silica gel binder is added) obtained in the comparative example 1 can obtain NO removal efficiency of more than 90% within 200-300 ℃, which shows that the molecular sieve catalytic inorganic fiber obtained by the preparation method of the invention has the advantage of wider catalytic temperature window.

The applicant declares that the present invention illustrates the detailed structural features of the present invention through the above embodiments, but the present invention is not limited to the above detailed structural features, that is, it does not mean that the present invention must be implemented depending on the above detailed structural features. It should be understood by those skilled in the art that any modifications of the present invention, equivalent substitutions of selected components of the present invention, additions of auxiliary components, selection of specific modes, etc., are within the scope and disclosure of the present invention.

The preferred embodiments of the present invention have been described in detail, however, the present invention 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 invention within the technical idea of the present invention, and these simple modifications are within the protective scope of the present invention.

It should be noted that the various technical features described in the above embodiments can be combined in any suitable manner without contradiction, and the invention is not described in any way for the possible combinations in order to avoid unnecessary repetition.

In addition, any combination of the various embodiments of the present invention is also possible, and the same should be considered as the disclosure of the present invention as long as it does not depart from the spirit of the present invention.