CN112717877A

CN112717877A - Adsorbing material and preparation method and application thereof

Info

Publication number: CN112717877A
Application number: CN201911031671.3A
Authority: CN
Inventors: 王海洋; 李�杰; 张信伟; 刘全杰; 韩照明
Original assignee: China Petroleum and Chemical Corp; Sinopec Dalian Research Institute of Petroleum and Petrochemicals
Current assignee: China Petroleum and Chemical Corp; Sinopec Dalian Research Institute of Petroleum and Petrochemicals
Priority date: 2019-10-28
Filing date: 2019-10-28
Publication date: 2021-04-30

Abstract

The invention discloses an adsorbing material and a preparation method and application thereof. The preparation method of the adsorbing material comprises the following steps: (1) adopting sugar solution to perform dipping treatment on the 5A molecular sieve, drying the dipped molecular sieve and roasting the dipped molecular sieve in an inert atmosphere; (2) carrying out nitrogen-containing compound solution dipping treatment on the material obtained in the step (1); (3) drying and roasting the material treated in the step (2); (4) and (4) treating the material treated in the step (3) in an ammonia and steam mixed atmosphere, and drying and roasting the treated material to obtain the modified 5A molecular sieve. The modified 5A molecular sieve prepared by the method has high adsorption capacity and higher adsorption effect on monomethyl isoparaffin.

Description

Adsorbing material and preparation method and application thereof

Technical Field

The invention relates to an adsorption material and a preparation method and application thereof, in particular to a modified 5A molecular sieve adsorption material with high adsorption capacity and a preparation method and application thereof.

Background

The main pore canal of the 5A molecular sieve is an internal pore volume of 0.776 nm³The size of the pore diameter of the cubic sodium lattice is about 0.5 nm, and molecules with the molecular diameter of less than 0.5 nm can be allowed to pass through. Due to the shape selective adsorption effect, the 5A molecular sieve is widely used in the separation process of normal alkane and non-normal hydrocarbon in various petroleum raw materials, and a fixed bed process of gas-solid adsorption and a simulated moving bed process of liquid-solid adsorption are formed.

The 5A molecular sieve is a high-efficiency adsorption material for selectively separating normal paraffin in naphtha fraction. Naphtha is a mixture of various hydrocarbons such as normal paraffin, isoparaffin, naphthene and aromatic hydrocarbon. For steam cracking ethylene, different types of hydrocarbons contribute differently to the ethylene production. The yield of ethylene is highest in normal paraffin, and then in naphthene and isoparaffin, and aromatic hydrocarbon does not contribute to the generation of ethylene. On the other hand, as a catalytic reforming raw material, the reaction speed of cyclodehydrogenation of normal alkane into aromatic hydrocarbon is slow, and the conversion rate is low. Therefore, the method for analyzing the normal paraffin in the naphtha by using the 5A molecular sieve adsorbent is an effective method for fully utilizing the naphtha.

Foreign UOP company and Exxonmobil company have conducted research work for separating normal paraffins and non-normal hydrocarbons in naphtha by using a 5A molecular sieve as an adsorbent, and have achieved highly effective research results. The university of eastern China developed a 5A molecular sieve fixed bed adsorption separation process based on the concept of molecular management, which was used as raw materials for preparing ethylene by steam cracking and catalytic reforming, respectively, and the comprehensive utilization value of naphtha was improved.

CN103170304A discloses a method for preparing a 5A molecular sieve for straight-chain alkane adsorption by adopting attapulgite. Calcining attapulgite at high temperature, soaking in hydrochloric acid solution, dissolving in sodium hydroxide aqueous solution, dissolving sodium hydroxide and sodium metaaluminate in water, mixing the two liquids rapidly, stirring vigorously to obtain milky colloid, crystallizing the colloid at 80-95 deg.C for 4-6 hr, cooling, filtering, washing to pH less than 9, and oven drying to obtain 4A molecular sieve powder; and finally, carrying out ion exchange on the molecular sieve and a calcium chloride solution to obtain the 5A molecular sieve. The 5A molecular sieve has a static saturated adsorption capacity for n-decane up to 0.0716g/g, and a static saturated adsorption capacity for n-pentadecane up to 0.123 g/g. The 5A molecular sieve is prepared by cheap and easily available attapulgite resources, replaces the traditional chemical raw material method, and has good saturated adsorption capacity to straight paraffin.

CN104045095A discloses a preparation method of a 5A molecular sieve. Adding tetraethoxysilane into a sodium hydroxide aqueous solution, stirring for a period of time, adding sodium metaaluminate into the water to be fully dissolved, quickly mixing the two liquids, violently stirring to obtain a milky colloid, crystallizing the colloid at the temperature of 80-95 ℃ for 4-6 hours, cooling, filtering, washing until the pH value is less than 9, and drying to obtain 4A molecular sieve raw powder; and finally, carrying out ion exchange on the molecular sieve and a calcium chloride solution to obtain the 5A molecular sieve. The 5A molecular sieve has a static saturated adsorption capacity of n-decane up to 0.538g/g and a static saturated adsorption capacity of n-pentadecane up to 0.647 g/g. The 5A molecular sieve is prepared by adopting an organic silicon source of tetraethoxysilane as a silicon source to replace inorganic silicon source of sodium silicate, so that the pore passages of the 5A molecular sieve have diversity and the molecular sieve has good saturated adsorption capacity on straight paraffin.

CN1530167A discloses a preparation method of a high-performance pressure swing adsorption 5A molecular sieve, which comprises the following process steps: (1) mixing 80-90 parts by weight of 4A molecular sieve raw powder and 5-20 parts by weight of kaolin clay, adding 1-50 parts by weight of additive plant fiber, and granulating in a high-speed granulator. (2) And screening the granulated intermediate product according to the fineness requirement of the product, drying, and roasting at a high temperature of 200-1000 ℃. (3) Immersing the intermediate product after roasting in 4-25 wt% sodium hydroxide solution for alkali treatment, washing, and adding 2-20 wt% CaCl₂Solution of Ca²⁺Exchanging, washing and drying, and then roasting the granular product for the second time at the temperature of 100-800 ℃ to obtain the high-performance pressure swing adsorption 5A molecular sieve product. The 5A molecular sieve prepared by the method has larger adsorption capacity, faster diffusion rate and higher mechanical strength, and is used for the aspects of pressure swing adsorption oxygen generation, hydrogen production, petroleum dewaxing and the like.

CN106861614A discloses a 5A molecular sieve adsorbent containing normal paraffin distillate oil for adsorptive separation and a preparation method thereof, the preparation method comprises the steps of adding polyquaternium as a crystallization synthesis soft template agent into a sol system mixed by a silicon source and an aluminum source, and hydrothermally synthesizing a hierarchical pore 4A molecular sieve with a micropore-mesopore structure; removing the soft template agent from the 4A molecular sieve, forming the 4A molecular sieve and a binder rolling ball into small balls with the particle size of 0.2-0.8 mm, drying, roasting, and then performing calcium ion exchange and activation to obtain a 5A molecular sieve adsorbent with a micropore-mesopore structure; in the adsorbent, the proportion of the 5A molecular sieve is 90-97 wt%, and the proportion of the binder is 3-10%. The multistage pore canal 5A molecular sieve synthesized by the method keeps higher equilibrium adsorption capacity to normal paraffin, and simultaneously remarkably improves the diffusion coefficient of the normal paraffin in the molecular sieve, thereby improving the speed of adsorption separation.

CN200510012550.6 a method for preparing a zeolite molecular sieve adsorbent with high adsorption quantity, belonging to the technical field of preparation and modification of zeolite molecular sieves. The method is characterized in that the method for preparing the zeolite molecular sieve adsorbent with high carbon monoxide adsorption quantity comprises the following steps: carrying out ion exchange on the binderless 4A molecular sieve and a calcium chloride solution to balance, washing with water, drying to prepare a 5A molecular sieve, then soaking with a dilute solution of sodium hydroxide or water glass, drying and activating to obtain the modified 5A molecular sieve adsorbent with high carbon monoxide adsorption capacity. The invention can obviously improve the adsorption performance of the 5A molecular sieve on carbon monoxide by modifying the molecular sieve by using an alkaline solution impregnation method, and the adsorption capacity of the modified adsorbent is improved by 1-15% compared with that before modification. The method is simple and easy to implement, low in cost and extremely wide in application prospect.

CN201510365330.5 discloses a modified 5A molecular sieve for removing a small amount of n-hexane in isohexane, which refers to that 5A molecular sieve to be modified is subjected to soaking dealumination treatment by using an ethanol solution of oxalic acid to obtain the modified 5A molecular sieve. Meanwhile, the invention discloses a regeneration method of the modified 5A molecular sieve after adsorbing n-hexane. The method has the advantages that: 1) the modified 5A molecular sieve has higher porosity and higher adsorption capacity to n-hexane, so that more isohexane (containing a small amount of n-hexane) can be treated; 2) the steam replacement method in the regeneration process avoids the phenomenon of carbon deposition caused by overhigh local temperature in the process of directly desorbing normal hexane by high-temperature decompression.

The 5A molecular sieve synthesized by the traditional method only has a micropore channel structure. The slow molecular diffusion rate and the long molecular diffusion path in the micropores lead to low utilization rate in the activity of the molecular sieve crystal, and greatly limit the rate of the adsorption/desorption process, so that the cycle period of adsorption/desorption is long. The molecular sieve is easy to be coked and blocked by impurities in the using process, so that a large number of pore passages are ineffective, and the effective utilization rate and the service life of the molecular sieve are seriously influenced. Meanwhile, a micro-channel system with a small pore diameter has the problem of poor separation effect on low-octane components formed by monomethyl isoparaffin.

Disclosure of Invention

Aiming at the defects of the prior art, the invention provides a modified 5A molecular sieve and a preparation method and application thereof. The modified 5A molecular sieve prepared by the method has high adsorption capacity and higher adsorption effect on monomethyl isoparaffin.

A preparation method of an adsorbing material comprises the following steps:

(1) adopting sugar solution to perform dipping treatment on the 5A molecular sieve, drying the dipped molecular sieve and roasting the dipped molecular sieve in an inert atmosphere;

(2) dipping the material obtained in the step (1) by adopting a nitrogen-containing compound solution;

(3) drying and roasting the material treated in the step (2);

(4) and (4) treating the material treated in the step (3) in an ammonia and steam mixed atmosphere, and drying and roasting the treated material to obtain the modified 5A molecular sieve.

In the above method, the 5A molecular sieve may be an existing commercial product, or may be prepared according to a method well known to those skilled in the art, for example, a calcium ion solution may be used to perform ion exchange with a 4A molecular sieve to prepare a 5A molecular sieve. The 5A molecular sieve can be prepared or selected from proper particle forms according to the use requirement, such as strips, tablets, columns, spheres and the like, and is preferably spherical. Shaping can be carried out according to the general knowledge in the art.

In the method, the sugar solution is a sugar aqueous solution, the mass concentration of sugar in the sugar solution is 5-35%, preferably 10-25%, and the sugar is one or more of fructose, glucose, sucrose and maltose.

In the above method, the impregnation may be over-volume impregnation or equal-volume impregnation, or one impregnation or multiple impregnations. The drying temperature after dipping is 90-150 ℃, the drying time is 0.5-6h, and the drying is preferably carried out for 1-4 h at 110-140 ℃. Roasting for 2-15 hours at 280-500 ℃ under the protection of nitrogen, preferably for 4-10 hours at 300-450 ℃.

In the method, the nitrogen-containing compound solution is soaked for 0.5-20 h, preferably for 1-10 h by using 1-50% by mass of nitrogen-containing compound solution at 80-250 ℃, preferably 120-180 ℃, the mass ratio of the nitrogen-containing compound solution to the 5A molecular sieve is 50: 1-2: 1, preferably 20: 1-5: 1, and the pressure treatment can be sealed and adjusted in order to control the appropriate temperature.

In the above method, the nitrogen-containing compound solution immersion treatment may be carried out under one temperature condition or may be carried out in a plurality of stages under different temperature conditions, preferably in a manner of high temperature treatment followed by low temperature treatment, and the temperature difference between the high temperature treatment and the low temperature treatment is 20 to 50 ℃. The preferable operation mode is that the dipping treatment is firstly carried out for 0.5 to 10 hours at the temperature of 150 to 250 ℃, and then the dipping treatment is carried out for 0.5 to 10 hours at the temperature of 90 to 120 ℃. The adsorption capacity of the modified 5A molecular sieve can be further improved by adopting a high-first-low sectional impregnation treatment mode.

In the method, the nitrogen-containing compound in the step (2) is preferably a basic nitrogen-containing compound, and mainly comprises amines, wherein the amines comprise one or more of aliphatic amine, alcohol amine, amide, alicyclic amine or aromatic amine. The composition specifically comprises one or more of monoethylamine, diethylamine, triethylamine, ethylenediamine, hexamethylenediamine, tert-butylamine, monoethanolamine, diethanolamine, triethanolamine, dimethylformamide, propionamide, butyramide, pyridine, morphine, aniline, diphenylamine, 1-naphthylamine and dinaphthylamine, and preferably one or more of monoethylamine, ethylenediamine and monoethanolamine.

In the method, the volume content of ammonia in the ammonia-steam mixed atmosphere is 10-45%, the treatment temperature is 120-150 ℃, and the treatment time is 0.5-6 h.

In the above method, the temperature for drying in step (3) or step (4) may be 50 to 200 ℃, preferably 60 to 150 ℃, and more preferably 80 to 120 ℃; the drying time is 1-24 h, preferably 4-8 h; the drying can be vacuum drying, or drying under the protection of inert gas, or drying in air atmosphere; the roasting temperature is 200-800 ℃, and preferably 400-600 ℃; the roasting time is 1-24 h, preferably 4-8 h; the carbon deposit is removed by roasting in an air atmosphere or an oxygen atmosphere.

A modified 5A molecular sieve prepared by the method. The modified 5A molecular sieve is used as an adsorbent for adsorption separation of normal paraffin in naphtha, and the specific separation process is as follows: taking naphtha containing 5-45% of normal alkane as a raw material in percentage by weight, and performing reaction at the temperature of 100-300 ℃ and the pressure of 0.1-2.5 Mpa in a bed layer and at the mass space velocity of 0.2-4 h^-1Under the condition of (1), the raw material is contacted with an adsorbent, wherein the used adsorbent particles are 1.6 mm-2.3 mm.

The method comprises the steps of firstly carrying out carbonization treatment on the outer surface of a 5A molecular sieve, wherein the purpose of the carbonization treatment is to stabilize the orifice on the outer surface of the 5A molecular sieve, then carrying out hydrothermal treatment on the 5A molecular sieve, carrying out pore expansion and modification treatment on the inner hole of the 5A molecular sieve, and finally carrying out proper pore expansion treatment on the surface orifice of the 5A molecular sieve, wherein the modified 5A molecular sieve is used as an adsorbent and has good adsorption selectivity on low-octane components such as normal alkane, methyl pentane and monomethyl hexane.

Detailed Description

The technical solution and the technical effects obtained by the method of the present invention will be further described below with reference to examples and comparative examples, but the following examples do not limit the method of the present invention.

Example 1

(1) An appropriate amount of spherical 5A molecular sieve ((commercial product, main properties are as follows: specific surface: 680 cm)²The pore volume per gram: 0.18cm³Per g, average pore diameter: 1.7nm, particle diameter: 1.6 mm-2.3 mm), adopting a glucose solution with the mass concentration of 10% to carry out protective impregnation treatment on the 5A molecular sieve, drying the 5A molecular sieve for 3h at 110 ℃ after impregnation, and roasting the 5A molecular sieve for 4h at 450 ℃ in a nitrogen atmosphere;

(2) dipping the material obtained in the step (1) by adopting a nitrogen-containing compound solution, namely an ethylene diamine aqueous solution, wherein the dipping condition of the nitrogen-containing compound solution is that 30% by mass of the nitrogen-containing compound solution is dipped for 8 hours at 120 ℃, and the mass ratio of the nitrogen-containing compound solution to the 5A molecular sieve is 5: 1;

(3) vacuum drying the filtered material in the step (2) at 120 ℃ for 4h, roasting at 600 ℃ for 4h, and roasting in an air atmosphere;

(4) treating the material treated in the step (3) in an ammonia and steam mixed atmosphere; the volume content of ammonia in the ammonia-steam mixed atmosphere is 20%, the treatment temperature is 150 ℃, the treatment time is 5 hours, the modified molecular sieve is dried in vacuum at 120 ℃ for 4 hours after treatment, and the modified molecular sieve is prepared by roasting at 600 ℃ in the air atmosphere for 4 hours.

Dynamic evaluation of the adsorbent on a fixed bed adsorption apparatus: the laboratory material is naphtha, wherein the total weight content of the normal paraffins from C4 to C8 is 21.25 percent, and the content of the monomethyl isoalkane is 11.16 percent; the experimental conditions are that the temperature of the adsorbent bed layer is 235 ℃, the pressure of the bed layer is 0.4Mpa, the packing content of the adsorbent is 25g, the height of the bed layer is 25cm, and the mass space velocity is 1.5h^-1Under the conditions, the raw material is contacted with an adsorbent, the content of normal paraffin in raffinate oil is 1wt% as a breakthrough point, the adsorption quantity of the normal paraffin in the naphtha at the breakthrough point (the main components are normal paraffin and monomethyl isoparaffin) and the content of the normal paraffin and the monomethyl isoparaffin in the adsorbed naphtha are measured, and the results are shown in table 1; and stopping feeding nitrogen to purge and desorb, and feeding and adsorbing after desorption.

Example 2

(1) An appropriate amount of spherical 5A molecular sieve ((commercial product, main properties are as follows: specific surface: 680 cm)²The pore volume per gram: 0.18cm³Per g, average pore diameter: 1.7nm, particle diameter: 1.6 mm-2.3 mm), and adopting sucrose solution with mass concentration of 25% to perform protective dipping treatment on the 5A molecular sieveDrying at 140 ℃ for 1h after impregnation, and roasting at 300 ℃ for 8h in a nitrogen atmosphere;

(2) and (2) soaking the material obtained in the step (1) by adopting a nitrogen-containing compound solution, namely a monoethylamine aqueous solution, wherein the nitrogen-containing compound solution is soaked for 10 hours by using a nitrogen-containing compound solution with the mass content of 10% at the temperature of 180 ℃, and the mass ratio of the nitrogen-containing compound solution to the 5A molecular sieve is 15: 1.

(3) Drying the filtered material at 80 ℃ for 8h in vacuum, roasting at 400 ℃ for 8h, and roasting in air atmosphere;

(4) treating the material treated in the step (3) in an ammonia and steam mixed atmosphere; the volume content of ammonia in the ammonia-steam mixed atmosphere is 40%, the treatment temperature is 120 ℃, the treatment time is 2 hours, the modified 5A molecular sieve is prepared by carrying out hydrothermal treatment, then carrying out vacuum drying for 4 hours at 120 ℃ and roasting for 4 hours at 600 ℃ in the air atmosphere.

Example 3

(1) An appropriate amount of spherical 5A molecular sieve ((commercial product, main properties are as follows: specific surface: 680 cm)²The pore volume per gram: 0.18cm³Per g, average pore diameter: 1.7nm, particle diameter: 1.6 mm-2.3 mm), performing protective impregnation treatment on the 5A molecular sieve by adopting a fructose solution with the mass concentration of 15%, drying at 125 ℃ for 2.5h after impregnation, and roasting at 380 ℃ for 6h under a nitrogen atmosphere;

(2) dipping the material obtained in the step (1) by adopting a nitrogen-containing compound solution, namely an ethanolamine aqueous solution, wherein the dipping condition of the nitrogen-containing compound solution is that a nitrogen-containing compound solution with the mass content of 5% is dipped for 5 hours at the temperature of 150 ℃, and the mass ratio of the nitrogen-containing compound solution to the 5A molecular sieve is 10: 1;

(3) vacuum drying the filtered material at 120 ℃ for 8h, roasting at 500 ℃ for 8h, and roasting in air atmosphere;

(4) treating the material treated in the step (3) in an ammonia and steam mixed atmosphere; the volume content of ammonia in the ammonia-steam mixed atmosphere is 30%, the treatment temperature is 135 ℃, the treatment time is 4 hours, the modified 5A molecular sieve is prepared by carrying out hydrothermal treatment, then carrying out vacuum drying for 4 hours at 120 ℃ and roasting for 4 hours at 600 ℃ in the air atmosphere.

Example 4

(1) An appropriate amount of spherical 5A molecular sieve ((commercial product, main properties are as follows: specific surface: 680 cm)²The pore volume per gram: 0.18cm³Per g, average pore diameter: 1.7nm, particle diameter: 1.6 mm-2.3 mm), adopting maltose solution with mass concentration of 18% to carry out protective impregnation treatment on the 5A molecular sieve, drying for 2.5h at 125 ℃ after impregnation, and roasting for 5h at 330 ℃ in nitrogen atmosphere;

(2) dipping the material obtained in the step (1) by adopting a nitrogen-containing compound solution, namely an ethylene diamine aqueous solution, wherein the dipping treatment condition of the nitrogen-containing compound solution is that under the condition of 80, the nitrogen-containing compound solution with the mass content of 40 is dipped for 0.5h, and the mass ratio of the nitrogen-containing compound solution to the 5A molecular sieve is 15: 1;

(3) vacuum drying the filtered material at 100 ℃ for 5h, roasting at 450 ℃ for 10h, and roasting in an air atmosphere;

(4) treating the material treated in the step (3) in an ammonia and steam mixed atmosphere; the volume content of ammonia in the ammonia-steam mixed atmosphere is 30%, the treatment temperature is 135 ℃, the treatment time is 4 hours, the modified 5A molecular sieve is prepared by carrying out hydrothermal treatment, then carrying out vacuum drying for 4 hours at 120 ℃ and roasting for 4 hours at 500 ℃ in the air atmosphere.

Example 5

(1) An appropriate amount of spherical 5A molecular sieve ((commercial product, main properties are as follows: specific surface: 680 cm)²The pore volume per gram: 0.18cm³Per g, average pore diameter: 1.7nm, particle diameter: 1.6 mm-2.3 mm), adopting a glucose solution with the mass concentration of 20% to carry out protective impregnation treatment on the 5A molecular sieve, drying for 3.5h at 130 ℃ after impregnation, and roasting for 8h at 360 ℃ in a nitrogen atmosphere;

(2) dipping the material obtained in the step (1) by adopting a nitrogen-containing compound solution, namely an ethylene diamine aqueous solution, wherein the dipping condition of the nitrogen-containing compound solution is that the nitrogen-containing compound solution with the mass content of 25% is dipped for 5 hours at the temperature of 150 ℃, and the mass ratio of the nitrogen-containing compound solution to the 5A molecular sieve is 25: 1;

(3) vacuum drying the filtered material at 110 ℃ for 5h, roasting at 450 ℃ for 10h, and roasting in air atmosphere;

Example 6

(1) An appropriate amount of spherical 5A molecular sieve ((commercial product, main properties are as follows: specific surface: 680 cm)²The pore volume per gram: 0.18cm³Per g, average pore diameter: 1.7nm, particle diameter: 1.6 mm-2.3 mm), adopting a glucose solution with the mass concentration of 22% to carry out protective impregnation treatment on the 5A molecular sieve, drying at 115 ℃ for 1.5h after impregnation, and roasting at 320 ℃ for 4h under a nitrogen atmosphere;

(2) dipping the material obtained in the step (1) by adopting a nitrogen-containing compound solution, namely an aqueous solution of monoethanolamine, wherein the dipping condition of the nitrogen-containing compound solution is that the nitrogen-containing compound solution with the mass content of 12% is dipped for 8 hours at the temperature of 140 ℃, and the mass ratio of the nitrogen-containing compound solution to the 5A molecular sieve is 10: 1;

(3) vacuum drying the filtered material at 100 ℃ for 5h, roasting at 430 ℃ for 10h, and roasting in an air atmosphere;

Example 7

(2) dipping the material obtained in the step (1) by adopting a nitrogen-containing compound solution, namely an ethylenediamine aqueous solution, wherein the mass content of ethylenediamine in the ethylenediamine aqueous solution is 30%, and the mass ratio of the ethylenediamine aqueous solution to the 5A molecular sieve is 5: 1; firstly, carrying out immersion treatment for 5h at 200 ℃, and then carrying out immersion treatment for 3h at 100 ℃;

(3) vacuum drying the filtered material at 120 ℃ for 4h, roasting at 600 ℃ for 4h, and roasting in air atmosphere;

Comparative example 1 [ same as example 1 except that step (4) was omitted ]

(3) and (3) drying the filtered material in the step (2) at 120 ℃ for 4h in vacuum, roasting at 600 ℃ for 4h, and roasting in an air atmosphere to obtain the modified molecular sieve.

Dynamic evaluation of the adsorbent on a fixed bed adsorption apparatus: the laboratory feed was naphtha containing 21.25% by weight of C4 to C8 normal paraffins and 11.1% by weight of monomethyl isoparaffins6 percent; the experimental conditions are that the temperature of the adsorbent bed layer is 235 ℃, the pressure of the bed layer is 0.4Mpa, the packing content of the adsorbent is 25g, the height of the bed layer is 25cm, and the mass space velocity is 1.5h^-1Under the conditions, the raw material is contacted with an adsorbent, the content of normal paraffin in raffinate oil is 1wt% as a breakthrough point, the adsorption quantity of the normal paraffin in the naphtha at the breakthrough point (the main components are normal paraffin and monomethyl isoparaffin) and the content of the normal paraffin and the monomethyl isoparaffin in the adsorbed naphtha are measured, and the results are shown in table 1; and stopping feeding nitrogen to purge and desorb, and feeding and adsorbing after desorption.

Comparative example 2

The 5A molecular sieve directly acts as an adsorbent. Dynamic evaluation of the adsorbent on a fixed bed adsorption apparatus: the laboratory material is naphtha, wherein the total weight content of the normal paraffins from C4 to C8 is 21.25 percent, and the content of the monomethyl isoalkane is 11.16 percent; the experimental conditions are that the temperature of the adsorbent bed layer is 235 ℃, the pressure of the bed layer is 0.4Mpa, the packing content of the adsorbent is 25g, the height of the bed layer is 25cm, and the mass space velocity is 1.5h^-1Under the conditions, the raw material is contacted with an adsorbent, the content of normal paraffin in raffinate oil is 1wt% as a breakthrough point, the adsorption quantity of the normal paraffin in the naphtha at the breakthrough point (the main components are normal paraffin and monomethyl isoparaffin) and the content of the normal paraffin and the monomethyl isoparaffin in the adsorbed naphtha are measured, and the results are shown in table 1; and stopping feeding nitrogen to purge and desorb, and feeding and adsorbing after desorption.

TABLE 1

Claims

1. A preparation method of an adsorbing material is characterized by comprising the following steps: the method comprises the following steps:

(3) drying and roasting the material treated in the step (2);

2. The method of claim 1, wherein: the 5A molecular sieves are currently commercially available products or are prepared according to methods well known to those skilled in the art.

3. The method of claim 1, wherein: the 5A molecular sieve is one of strip, plate, column or sphere.

4. The method of claim 1, wherein: the sugar solution is a sugar water solution, and the mass concentration of sugar in the sugar solution is 5-35%.

5. The method of claim 4, wherein: the mass concentration of sugar in the sugar solution is 10-25%.

6. The method of claim 1, wherein: the sugar is one or more of fructose, glucose, sucrose and maltose.

7. The method of claim 1, wherein: drying at 90-150 ℃ for 0.5-6h after dipping in the step (1); roasting for 2-15 hours at 280-500 ℃ under the protection of nitrogen.

8. The method of claim 7, wherein: drying after dipping in the step (1) is carried out for 1-4 h at 110-140 ℃, and roasting is carried out for 4-10 h at 300-450 ℃ under the protection of nitrogen.

9. The method of claim 1, wherein: the impregnation in the step (1) adopts overbody impregnation or isovolumetric impregnation.

10. The method of claim 1, wherein: the nitrogen-containing compound solution is soaked for 0.5-20 hours at 80-250 ℃ by using a nitrogen-containing compound solution with the mass content of 1-50%, and the mass ratio of the nitrogen-containing compound solution to the 5A molecular sieve is 50: 1-2: 1.

11. The method of claim 10, wherein: the nitrogen-containing compound solution is soaked for 1-10 hours at 120-180 ℃ by using a nitrogen-containing compound solution with the mass content of 5-30%, and the mass ratio of the nitrogen-containing compound solution to the 5A molecular sieve is 20: 1-5: 1.

12. The method of claim 1, wherein: the nitrogen-containing compound solution is dipped and treated by adopting a mode of firstly treating at high temperature and then treating at low temperature, and the temperature difference between the high-temperature treatment and the low-temperature treatment is 20-50 ℃.

13. The method of claim 11, wherein: firstly, dipping for 0.5-10 h at 150-250 ℃, and then dipping for 0.5-10 h at 90-120 ℃.

14. The method of claim 1, wherein: in the step (2), the nitrogen-containing compound is a basic nitrogen-containing compound, and the basic nitrogen-containing compound is one or more of aliphatic amine, alcohol amine, amide, alicyclic amine or aromatic amine.

15. The method of claim 14, wherein: the nitrogen-containing compound is one or more of monoethylamine, diethylamine, triethylamine, ethylenediamine, hexanediamine, tert-butylamine, monoethanolamine, diethanolamine, triethanolamine, dimethylformamide, propionamide, butyramide, pyridine, morphine, aniline, diphenylamine, 1-naphthylamine and dinaphthylamine.

16. The method of claim 15, wherein: the nitrogen-containing compound is one or more of monoethylamine, ethylenediamine and monoethanolamine.

17. The method of claim 1, wherein: the volume content of ammonia in the ammonia-steam mixed atmosphere is 10-45%, the treatment temperature is 120-150 ℃, and the treatment time is 0.5-6 h.

18. The method of claim 1, wherein: the drying temperature is 50-200 ℃; the drying time is 1-24 h; the roasting temperature is 200-800 ℃; the roasting time is 1-24 h.

19. A modified 5A molecular sieve whenever prepared by a process as claimed in any one of claims 1 to 18.

20. The modified 5A molecular sieve of claim 19 as an adsorbent for use in adsorptive separation of naphtha.

21. Use according to claim 20, characterized in that: the specific separation process is as follows: taking naphtha as a raw material, and performing a bed temperature of 100-300 ℃, a bed pressure of 0.1-2.5 Mpa and a mass space velocity of 0.2-4 h^-1Under the conditions of (1), the raw material is contacted with the adsorbent.