阅读说明：本技术 一种两亲性多孔环糊精聚合物 (Amphiphilic porous cyclodextrin polymer ) 是由 谢显传 屠一舟 于 2019-10-11 设计创作，主要内容包括：本发明提供一种两亲的多孔环糊精聚合物：将环糊精接枝芳香类分子,再与联苯二氯苄和对二氯苄通过傅克烷基化反应,得到具有超高比表面的多孔聚合物。该材料具有非常高的吸附容量,再生简单,可重复利用。由于环糊精的羟基被部分保留下来,提高了材料表面的亲水性,使其吸附速率快,且具有多种吸附机理,并能同时吸附疏水性和亲水性污染物。(The present invention provides an amphiphilic porous cyclodextrin polymer: the cyclodextrin is grafted with aromatic molecules, and then the aromatic molecules, biphenyl dichlorobenzyl and p-dichlorobenzyl are subjected to Friedel-crafts alkylation reaction to obtain the porous polymer with the ultrahigh specific surface. The material has very high adsorption capacity, simple regeneration and reusability. Because the hydroxyl of the cyclodextrin is partially reserved, the hydrophilicity of the surface of the material is improved, the adsorption rate of the material is high, the material has multiple adsorption mechanisms, and hydrophobic and hydrophilic pollutants can be adsorbed simultaneously.)

1. A preparation method of amphiphilic cyclodextrin porous polymer is characterized in that,

the cyclodextrin is grafted with an aromatic compound,

cross-linking with alkylating reagent under the condition of using Lewis acid as catalyst,

the BET specific surface area of the cyclodextrin porous polymer measured by a nitrogen isotherm method is 1200m² g^-1The above.

2. The method of claim 1, wherein the aromatic compound is a halogenated aromatic compound.

3. The method according to claim 1 or 2, wherein the aromatic compound is a benzylating agent.

4. The process according to claim 3, wherein the molar ratio of benzylating agent to cyclodextrin ranges from 3 to 7: 1.

5. the process of claim 1, wherein the alkylating agent is one or a combination of 2 or more of alkylating agents containing benzene rings.

6. The method of claim 5, wherein the alkylating agent containing a benzene ring structure is selected from the group consisting of p-dichlorobenzyl, biphenyl dichlorobenzyl, p-dibromide benzyl, and biphenyl dibromide benzyl.

7. The process according to claim 6, wherein the molar ratio of alkylating agent to benzylated cyclodextrin is from 5 to 8: 1.

8. the process according to claim 1, wherein the Lewis acid is a metal chloride or sulfuric acid.

9. The method of any one of claims 1 to 8, comprising the steps of:

a. grafting cyclodextrin with halogenated aromatic compound:

dissolving cyclodextrin, cooling in ice water bath, adding sodium hydride, stirring, slowly dropping the grafting reagent, heating to room temperature, stirring overnight,

reacting overnight to obtain a light yellow solution, adding methanol to quench and terminate the reaction,

adding distilled water, mixing, continuously extracting with dichloromethane for three times, drying, filtering, and rotary evaporating at the boiling point of dichloromethane to obtain light yellow solution;

b. polymerization reaction:

dissolving benzylated cyclodextrin and an alkylating reagent, slowly adding Lewis acid as a catalyst under the protection of nitrogen for reaction,

a brown precipitate is obtained, which is washed with methanol and water until the filtrate is neutral and colorless, subjected to Soxhlet extraction with methanol, dried in a vacuum drying oven, and ground and sieved to obtain a brown powder.

10. An application of amphiphilic cyclodextrin porous polymer in adsorbing and enriching organic micropollutants is characterized in that,

the cyclodextrin porous polymer is obtained by grafting an aromatic compound onto cyclodextrin, and crosslinking the aromatic compound with an alkylating reagent under the condition of taking Lewis acid as a catalyst,

the BET specific surface area of the cyclodextrin porous polymer measured by a nitrogen isotherm method is 1200m² g^-1The above.

Technical Field

The invention relates to the technical field of environment-friendly materials, in particular to a method for preparing an amphiphilic cyclodextrin polymer with a high specific surface area and application thereof.

Background

Organic micropollutants are complex in type and vary in nature, including hydrophobic and hydrophilic contaminants, and their removal by conventional biological treatment is often limited, adsorption is the more common method, and many adsorbents do not exhibit good results for the removal of hydrophilic contaminants. The activated carbon is used as the most widely used adsorbent in the industry at present, but has the defects of high regeneration energy consumption, low repeated utilization rate and the like. In addition, the adsorption rate of activated carbon is slow, it takes a long time to reach equilibrium, and its adsorption effect is often affected by the water solubility of the contaminants, which limits its further applications.

Cyclodextrin (CD) is prepared by the action of cyclodextrin glucosyltransferase on starch. The cyclodextrin material has the advantages of low cost, good adsorption performance and good regeneration performance, and is a potential novel adsorbent. Its unique hydrophobic cavity and hydrophilic outer lining can encapsulate organic contaminants by a host-guest mechanism. In addition, the CD molecules have high reactivity, a large number of hydroxyl groups are arranged at two ends of each CD molecule, and the CD molecules can be crosslinked with different crosslinking agents to form a macromolecular network and have an adsorption effect on pollutants. However, the cyclodextrin polymers reported at present have very low specific surface areas (1-10 m)² g^-1) The pore structure is less, which limits its industrial application.

The Friedel-crafts alkylation reaction is often used for preparing the ultrahigh cross-linked polymer and has the characteristics of simple synthesis process, porous material, no toxicity, good thermal stability and the like. However, ultra-highly crosslinked polymers tend to be very hydrophobic and have low density and are typically used for gas adsorption, and poor wetting limits their use in water treatment. Therefore, the synthesis of an amphiphilic ultra-high cross-linked cyclodextrin material, in particular an ideal material with high specific surface area, large adsorption capacity, fast adsorption rate, good reproducibility and low cost, becomes a new subject.

Patent document 1 also discloses a cyclodextrin derivative, but patent document 1 completely substitutes a benzyl group with cyclodextrin, and then further modifies the cyclodextrin by removing one to two benzyl groups from a hydroxyl group at a specific position. The method directly controls the charge ratio of the grafting reaction, has low substitution degree, and obtains an intermediate which has a large amount of benzyl groups for providing reaction sites of the next step and simultaneously reserves a large amount of hydroxyl groups. Alkylation reaction of the last stepThe polymer obtained by the present invention has the structure of (BnO) x- (HO) y-CD- [ C₁₄H₁₂]z-[C₈H₈]_rWherein x + y is 21, and z and r are natural numbers. The structure obtained in patent document 1 is, for example, (BnO) m-CD- [ CH₂-O-R₄-CN]n, except that the reactive sites of the latter are all such that the hydroxyl groups of the cyclodextrin form ether linkages and m + n is 21 (fully substituted), the resulting material being an intermediate. The former retains hydroxyl groups, x < 21, (low degree of substitution), and the alkylation reaction site is on the aromatic ring of the benzyl group, the final synthetic material is a high polymer rather than an intermediate. Based on the difference, because the final material contains a large amount of benzyl, hydroxyl and a cross-linking agent containing a benzene ring, in the polymerization process, the rigid structures provide favorable conditions for pore-forming and provide a large amount of hydrophobic effect; while the large number of hydroxyl groups renders the material hydrophilic, providing hydrogen bonding upon adsorption of contaminants. The combination of the two makes the material have obvious advantages for the adsorption of organic matters.

In addition, the synthesis method has the idea that all three hydroxyl groups on 2, 3 and 6 positions of cyclodextrin are benzylated, then the benzyl group on the 6-position hydroxyl group is acetylated due to different reactivity of the three hydroxyl groups, and then the benzyl group is hydrolyzed into the hydroxyl group. Further modification is performed on the hydroxyl groups. According to the invention, benzyl is directly grafted on part of hydroxyl groups of cyclodextrin, then a reaction site is provided by an aromatic ring on the benzyl, and the benzyl and a cross-linking agent are further subjected to polymerization reaction to obtain the porous cyclodextrin polymer with a high specific surface. The difference from the above synthetic thought lies in:

1. the purpose of benzylation is different, and in the synthesis thought, in order to protect the 6-position hydroxyl group on cyclodextrin; the invention aims to provide a polymerization reaction site, and the benzyl group contains a rigid structure of a benzene ring, so that the method is beneficial to pore forming in the subsequent polymerization reaction process.

2. The synthetic reaction sites are different, and the reaction site finally modified in the synthetic thought is still hydroxyl obtained through protection; the site of the polymerization reaction of the invention is an aromatic ring on a benzyl group;

3. the obtained products are different, and an intermediate is obtained by chemically modifying cyclodextrin hydroxyl in the synthesis thought; according to the invention, benzyl is grafted on cyclodextrin, then an amphiphilic high-molecular porous polymer with a high specific surface is obtained through polymerization reaction, and the amphiphilic high-molecular porous polymer is applied to removal of organic pollutants in a water body, and the two effects and properties are completely different.

Documents of the prior art

Patent document 1: WO2011/117317

Non-patent documents:

1.Wood,C.D.；Tan,B.；Trewin,A.；Su,F.；Rosseinsky,M.J.；Bradshaw,D.；Sun,Y.；Zhou,L.；Cooper,A.I.,Microporous Organic Polymers for Methane Storage.Advanced Materials 2008,20,(10),1916-1921.

2.Schute,K.；Rose,M.,Metal-free and Scalable Synthesis of Porous Hyper-cross-linked Polymers:Towards Applications in Liquid-Phase Adsorption.ChemSusChem 2015,8,(20),3419-23.

3.Li,H.；Meng,B.；Chai,S.H.；Liu,H.；Dai,S.,Hyper-crosslinked beta-cyclodextrin porous polymer:an adsorption-facilitated molecular catalyst support for transformation of water-soluble aromatic molecules.Chem Sci 2016,7,(2),905-909.

4.Alsbaiee,A.；Smith,B.J.；Xiao,L.；Ling,Y.；Helbling,D.E.；Dichtel,W.R.,Rapid removal of organic micropollutants from water by a porous beta-cyclodextrin polymer.Nature 2016,529,(7585),190-4.

disclosure of Invention

Technical problem to be solved by the invention

The invention provides a method for preparing a porous polymer with a high specific surface by benzylating cyclodextrin and crosslinking the benzylated cyclodextrin with an alkylating reagent with a rigid structure on the basis of the research of predecessors. Through adjusting the benzylation ratio of the cyclodextrin, a large number of hydroxyl groups on the cyclodextrin are reserved, and the hydrophilicity of the surface of the material is adjusted, so that the prepared cyclodextrin polymer material has very quick adsorption performance on organic pollutants in a water body, the removal rate of 1 minute reaches over 95 percent, and the cyclodextrin polymer material has very high adsorption capacity which is over 2 times that of activated carbon and is over 4 times that of EPI-CDP. And the polymer can adsorb hydrophobic contaminants and hydrophilic contaminants simultaneously due to the simultaneous action of multiple adsorption mechanisms, including hydrophobic, cyclodextrin inclusion and interaction, and hydrogen bonding.

The technical scheme of the invention is as follows:

preparing a cyclodextrin porous polymer with high specific surface area, grafting an aromatic compound onto cyclodextrin, and then crosslinking with an alkylating reagent at a certain temperature by using Lewis acid as a catalyst. And after the reaction is finished, filtering, washing for many times by using water and methanol in sequence, and drying to obtain the porous polymer with high specific surface.

The cyclodextrin polymer, grafted aromatic compound is halogenated compound. This is because, during the grafting reaction, it is preferable to replace the hydrogen atom on the hydroxyl group of cyclodextrin with sodium hydride and then add the halogenated aromatic compound, and the reaction scheme is as follows.

The cyclodextrin polymer, grafted halogenated compound is preferably a benzylating agent. The benzylation reaction has mild conditions, can react at room temperature and is rapid.

In the cyclodextrin polymer, the benzylation reagent is one or a combination of benzyl bromide and benzyl chloride.

In the cyclodextrin polymer, 21 hydroxyl groups exist in cyclodextrin, and in order to control the benzylation ratio, the molar ratio of the benzylation agent to the cyclodextrin is 1-21: 1. wherein the preferable ratio is 3-7: 1, more preferably 7: 1. this is due to the comparison of specific surface area and contact angle after cross-linking with different degrees of benzylation, the higher specific surface area after cross-linking with low benzylation cyclodextrins and the change of the surface of the material from superhydrophobic (contact angle 118.3 °) to hydrophilic (contact angle 7.8 °). This is because the low benzylated cyclodextrins, when crosslinked, have a low steric hindrance, which results in more micropores and thus a larger specific surface area. Meanwhile, a large amount of hydroxyl groups are reserved, so that the hydrophilicity of the surface is improved, the wettability of the material in liquid phase adsorption is greatly increased, and the adsorption and external diffusion process is promoted, so that the material has ultrahigh adsorption rate.

In the cyclodextrin polymer, the alkylating agent is one or a combination of alkylating agents containing benzene rings. The reason is that a large number of benzene rings in the polymer can generate strong hydrophobic effect due to the introduction of the benzene rings with rigid structures, and have important influence on the adsorption and enrichment of organic matters.

The above cyclodextrin polymer, wherein the alkylating agent having a benzene ring structure is selected from the group consisting of p-dichlorobenzyl, biphenyl dichlorobenzyl, p-dibromide benzyl, biphenyl dibromide benzyl, and combinations thereof. The combination of biphenyl dichlorobenzyl and p-dichlorobenzyl is preferred, and the obtained specific surface area is 1273-one 1445m² g^-1Compared with the use of a single cross-linking agent (710-1061 m)² g^-1) A higher specific surface area can be obtained.

The molar ratio of the alkylating agent to the benzylated cyclodextrin of the cyclodextrin polymer is 5-8: 1;

the Lewis acid used in the cyclodextrin polymer is one of metal chloride and sulfuric acid. The Friedel-crafts alkylation reaction process is as follows: the alkylating reagent generates carbonium ions under the action of Lewis acid catalyst, and then the carbonium ions and the electron-rich aromatic ring generate electrophilic reaction to generate alkylated products.

The metal chloride used in the cyclodextrin polymer is one of ferric trichloride and aluminum trichloride. Ferric trichloride is preferred because it possesses better water resistance than aluminum trichloride.

The cyclodextrin polymer with high specific surface area can be used as an adsorbent to remove organic micropollutants in water and can also be used as a pretreatment material to perform enrichment extraction on low-concentration organic micropollutants in water.

Furthermore, the organic micro-pollutants have better enrichment and removal effects on aromatic compounds.

The invention has the beneficial effects that: compared with the prior art, the preparation method of the invention has the advantages that the prepared material has 1445m² g^-1The specific surface area of the micropores reaches 523m² g^-1And has good thermal stability with only 5% mass loss at 275 ℃. In addition, the hydrophilicity and hydrophobicity of the surface of the material can be changed by adjusting the proportion of benzylation so as to be applied to different occasions. For example, the benzylation ratio is 7: 1, because the hydroxyl on the cyclodextrin is partially reserved, the hydrophilicity of the material is enhanced, and the adsorption process in a liquid phase is facilitated, so that the material has ultrahigh adsorption rate, and the removal rate can reach more than 95% in 1 minute. While higher benzylation ratios, such as 14:1 and 21:1, can be used for gas adsorption where moisture interference needs to be removed due to the highly hydrophobic surface of the prepared material. Meanwhile, the material has amphipathy, and because the material contains a large number of hydrophobic groups and a large number of hydrophilic hydroxyl groups, the material has the combined action of multiple adsorption mechanisms, so that the material can adsorb hydrophobic and hydrophilic pollutants simultaneously.

Drawings

FIG. 1: and (3) partially benzylating the beta-cyclodextrin, and then crosslinking the beta-cyclodextrin with biphenyl dichlorobenzyl and p-dichlorobenzyl to obtain a synthesis route map of the cyclodextrin porous polymer with high specific surface.

FIG. 2: contact angle plot of PBCD-B-D in example 1, characterizing hydrophobicity.

FIG. 3: the nitrogen adsorption isotherms, specific surfaces, pore size profiles, etc. of PBCD-B-D in example 1 and example 2.

FIG. 4: thermogravimetric analysis and infrared spectroscopy of PBCD-B-D in example 1.

FIG. 5: scanning electron micrographs and transmission electron micrographs of PBCD-B-D in example 1.

FIG. 6: adsorption kinetics of PBCD-B-D in example 1 and comparative examples 1 and 2 for selected contaminants are shown.

FIG. 7: the adsorption isotherm plots of PBCD-B-D in example 1 versus comparative examples 1 and 2 for selected contaminants.

FIG. 8: the regeneration performance of PBCD-B-D in example 1 was investigated.

Detailed Description

The specific method and the apparatus for characterizing the material are as follows:

physical chemical adsorption instrument: ASAP 2020(Micromeritics, USA). The nitrogen adsorption isotherm, specific surface area and pore size distribution of the material were determined.

An infrared measuring instrument: TENSOR 27(BRUKER, Germany).

An element analyzer: elementar variao EL cube (Elementar, Germany). The content of CHNO element in the material is measured. The polymer composition was investigated.

A thermal analyzer: pyris 1DSC (PerKinElmer, USA). The thermal stability of the material was investigated by thermogravimetric curves.

Scanning electron microscope: FEI QUANTA 250FEG (FEI, USA). The surface gold spraying treatment is carried out before the sample is tested to increase the conductivity of the sample.

Transmission electron microscopy: JEM-2100F (JEOL, Japan).

Contact angle measuring instrument: DSA100(Kruss, Germany).

Example 1:

preparation of porous cyclodextrin polymers:

dissolving cyclodextrin, and cooling in ice water bath; adding sodium hydride and stirring uniformly; slowly dripping a benzylation reagent into the mixture, and reacting the mixture overnight to obtain the benzylation cyclodextrin. The molar ratio of benzylating agent to cyclodextrin is shown in the example summary table below. Then the benzylated cyclodextrin reacts with an alkylating reagent for a certain time at a certain rotating speed and temperature in an oil bath kettle with magnetic stirring under the protection of nitrogen by the catalysis of Lewis acid. The molar ratio of alkylating agent to benzylated cyclodextrin is 5-8: 1. the temperature is generally from 55 to 100 ℃ and preferably from 75 to 90 ℃. The reaction time is preferably 15 to 30 hours, preferably 19 to 25 hours, most preferably 19 hours. If the amount is outside the above preferable range, the reaction may be incomplete, and the yield may be low. Washing the obtained product with distilled water and methanol for several times, performing Soxhlet extraction with methanol, and drying under vacuum to obtain the novel cyclodextrin material.

Chemical reagents and materials: all samples in the summary of examples were synthesized using the same conditions. Wherein the cyclodextrin is one of alpha, beta and gamma cyclodextrin; the benzylation reagent is one of benzyl bromide and benzyl chloride; alkylating to be one or a combination of biphenyl dichlorobenzyl and p-dichlorobenzyl; the Lewis acid is metal chloride or sulfuric acid, and the metal chloride is one of aluminum trichloride and ferric trichloride.

The ratio of the benzylation agent to the cyclodextrin will change the hydrophilicity and hydrophobicity of the material surface, and in order to obtain different samples, on the basis of example 1, the ratio of the benzylation agent to the cyclodextrin is adjusted as shown in table 1, and the obtained polymer is tested, and the results are shown in table 1.

Table 1 shows that the cyclodextrin with low degree of benzylation has a larger specific surface area after cross-linking, because the cyclodextrin with low degree of benzylation has less steric hindrance during cross-linking reaction, and well inhibits the generation of mesopores, thereby obtaining more micropores and a larger specific surface area; and because the hydroxyl is partially reserved, the hydrophilicity is improved, the wettability of the material surface is enhanced, the outer diffusion process in adsorption is improved, the adsorption rate is obviously increased, and the removal rate can reach 95 percent within 1 minute. The molar ratio of benzylating agent to cyclodextrin ranges from 1: 1-21: 1, preferably in a ratio of 3 to 7: 1, more preferably 7: 1.

TABLE 1

As shown in table 2, the polymers obtained from different types of cyclodextrin were also analyzed, and table 2 shows that α, β, and γ cyclodextrins can obtain large specific surface area and good adsorption effect after cross-linking.

TABLE 2

Table 3 is for the purpose of analyzing the influence of different catalysts, and the results are shown in Table 3. Table 3 shows that the reaction can be completed by using metal chloride and sulfuric acid as catalysts, and that ferric trichloride is preferred because aluminum trichloride absorbs water more easily. When sulfuric acid is used as a catalyst, the water resistance of the reaction can be improved, but the obtained specific surface area is lower; benzyl bromide and benzyl chloride can be used as benzylation reagents to achieve good effect.

TABLE 3

Table 4 shows that the polymers obtained with different cross-linking agents have different specific surface areas and different adsorption effects, and the best effect is obtained with the combination of BCMBP and DCX; next BCMBP and finally DCX.

TABLE 4

The table is consistent with the meaning and explanation as follows:

^amolar ratio of benzylating agent to cyclodextrin

^bSpecific surface area unit: m is² g^-1

BnBr: benzyl bromide

BnCl: benzyl chloride

BCMBP: biphenyl dichloro benzyl

DCX: p-dichloro benzyl

FeCl₃: ferric chloride

AlCl₃: aluminium trichloride

Quickly: the adsorption balance is achieved within 5 min;

and (3) the method is quick: the adsorption balance is reached within 10 min;

and (3) slow: the adsorption balance is reached within 20 min;

very slowly: the adsorption equilibrium is reached within 30 min.

In order to better explain the synthesis method of the present invention, the number 1(PBCD-B-D) will be specifically explained below.

Preparing an amphiphilic cyclodextrin polymer PBCD-B-D with high specific surface area:

preparation of partially benzylated cyclodextrin PBCD

Dissolving 2g of beta-cyclodextrin in 40mL of anhydrous dimethylformamide in a round-bottom flask, cooling the reaction bath to 0 ℃ at a low temperature and a constant temperature, adding 0.59g of 60% sodium hydride, and stirring for 15 min;

slowly dripping 0.8mL of benzyl bromide into the solution by using a constant-pressure funnel, heating to room temperature, and stirring overnight;

after reacting overnight, adding 5mL of methanol to quench and terminate the reaction;

100mL of distilled water was added and extracted three times with 50mL of methylene chloride in succession. The resulting solution was dried over anhydrous sodium sulfate, filtered and concentrated at 35 ℃ using a rotary evaporator to give partially benzylated cyclodextrin PBCD.

Preparation of PBCD-B-D

1) 1.06g of PBCD, 0.82g of biphenyl dichlorobenzyl and 0.19g of p-dichlorobenzyl are taken in a thick-walled pressure-resistant bottle, dissolved by 40mL of anhydrous 1, 2-dichloroethane, and 4.12g of anhydrous ferric chloride is slowly added under the protection of nitrogen. Heated to 80 ℃ and reacted for 19 h.

2) After the reaction was complete, the brown precipitate was collected and washed with water and methanol until the filtrate was neutral and colorless. Soxhlet extraction with methanol for 24h, drying in a vacuum drying oven at 50 ℃ for 24h, grinding and sieving to obtain PBCD-B-D as brown powder.

Example 2:

the sulfuric acid route is used for preparing a cyclodextrin polymer PBCD-B-D-H with a high specific surface area:

a. preparation of partially benzylated cyclodextrin PBCD

1) Dissolving 2g of beta-cyclodextrin in 40mL of anhydrous dimethylformamide in a round-bottom flask, cooling the reaction bath to 0 ℃ at a low temperature and a constant temperature, adding 0.59g of 60% sodium hydride, and stirring for 15 min;

2) slowly dripping 0.8mL of benzyl bromide into the solution by using a constant-pressure funnel, heating to room temperature, and stirring overnight;

3) after reacting overnight, adding 5mL of methanol to quench and terminate the reaction;

4) 100mL of distilled water was added and extracted three times with 50mL of methylene chloride in succession. The resulting solution was dried over anhydrous sodium sulfate, filtered and concentrated at 35 ℃ using a rotary evaporator to give partially benzylated cyclodextrin PBCD.

Preparation of PBCD-B-D-H

1) 1.06g of PBCD, 0.82g of biphenyldichlorobenzyl and 0.19g of p-dichlorobenzyl were taken out in a three-necked flask, dissolved in 20mL of anhydrous 1, 2-dichloroethane, and slowly added with 5mL of 98% sulfuric acid. The reaction was heated to 84 ℃ and reacted for 19h with reflux.

2) After the reaction was completed, the brown precipitate was collected, and washed with water and ethanol until the filtrate was neutral and colorless. Drying in a vacuum drying oven at 50 ℃ for 24H, grinding and sieving to obtain PBCD-B-D-H as brown powder.

Comparative example 1: preparation of nonporous beta-cyclodextrin polymer EPI-CDP:

EPI-CDP is the most widely used cyclodextrin polymer, but has the disadvantages of less pore structure and small adsorption capacity. Compared with the prior art, the invention has the advantages of high 1445m² g^-1The specific surface area of the catalyst is high, the adsorption rate is ultrahigh, and the removal rate of 1 minute reaches more than 95%.

EPI-CDP was prepared according to the method reported by Alsbaiee et al.

(1) 3g of beta-cyclodextrin were weighed into a round-bottomed flask, 5ml of 6.25mol L were added^-1NaOH lye to make the beta-cyclodextrin completely dissolved in the solution. (2) And (3) putting the flask into an oil bath kettle, adjusting the temperature to 60 ℃, controlling the rotation speed to be 120rpm, dropwise adding 2.5mL of epoxy chloropropane solution, and reacting for 1h after the dropwise adding is finished. (3) And collecting white gel obtained after the reaction is finished, filtering the white gel into a beaker, and purifying and washing the white gel for 3-4 times by using distilled water, tetrahydrofuran and dichloromethane in sequence. (4) Vacuum-pumping and freeze-drying the purified product at 50 ℃ for 12-24h, and (5) grinding the prepared nonporous beta-cyclodextrin polymer EPI-CDP into powder (60-80 meshes) for later use.

Comparative example 2: granular Activated Carbon (GAC)

The most widely used adsorbents are used in water treatment. Has a large number of microporous structures, but has the defects of slow adsorption rate, no balance within 30 minutes, large regeneration energy consumption and the like. Granular activated carbon (DARCO-AC,12-20 mesh) was purchased from Sigma and used after grinding to a fine powder (60-80 mesh). Compared with the prior art, the invention has the advantages of high 1445m² g^-1The specific surface area of the catalyst is high, the adsorption rate is ultrahigh, and the removal rate of 1 minute reaches more than 95%.

Example 3:

in order to fully illustrate the material performance of the amphiphilic high-specific-surface-area cyclodextrin polymer PBCD-B-D prepared in example 1, four model pollutants (3-phenylphenol, 2-naphthol, p-nitrophenol and p-chlorophenol) with different water solubility are selected to carry out adsorption experiments by taking activated carbon GAC and nonporous cyclodextrin polymer EPI-CDP as comparison materials, and the specific method is as follows:

the adsorbents used were ground to powders (60-80 mesh) prior to use. The sample taken was filtered through an Agilent 0.22 μm PTFE-Q filter (almost without adsorption of the above contaminants). The concentrations of the different contaminants in the water samples were then determined by High Performance Liquid Chromatography (HPLC). The chromatographic column adopts Agilent XDB-C18 analytical column (5 μm,4.6 × 250 mm), and the detector is ultraviolet detector.

The specific method for measuring the adsorption isotherm comprises the following steps: pouring 10mg of adsorbent into 40mL of prepared L with concentration range of 0.1-2.4mmol^-1Of the contaminant solution of (a). The reaction was carried out at 20 ℃ and 150rpm for 12 h. The adsorption capacity adopts the following formula:

wherein q is_e(mmol g^-1) For the amount of contaminants adsorbed per g, C₀(mmol L^-1) And C_e(mmol L^-1) Respectively, the initial concentration and the residual concentration of the contaminant. m (g) is the mass of the adsorbent and V (L) is the volume of the aqueous contaminant solution.

The specific method of the adsorption kinetics experiment comprises the following steps: pouring 10mg of adsorbent into 40ml of prepared 0.1mmol L^-1Of the contaminant solution of (a). Under magnetic stirring, a small amount of water sample is taken at regular intervals by using an injector, filtered by using a filter membrane and measured by using HPLC. The removal rate of contaminants in the solution was calculated using the following formula:

in the formula: c₀(mmol l^-1) And C_e(mmol l^-1) The original and residual concentrations of contaminants in the solution, respectively.

The following research results of adsorption experiments on different water-soluble pollutants show that PBCD-B-D has very high adsorption efficiency on all pollutants to be researched, and the removal efficiency in 1 minute can reach more than 95%. In addition, PBCD-B-D has adsorption capacity of over 2 times that of activated carbon and over 4 times that of EPI-CDP for all the pollutants, and has less influence on water solubility of the pollutants. The kinetic results are shown in FIG. 6, and the adsorption isotherm results are shown in FIG. 7.

(1) 3-Phenylphenol (C)_s：0.14g L^-1)

At an initial concentration of 2.4mmol L^-1When the adsorption capacity is balanced, PBCD-B-D has an equilibrium adsorption capacity of 3.38mmol g^-1Twice as much as GAC (1.52mmol g)^-1) Four times that of EPI-CDP (0.77mmol g)^-1). The removal rate of PBCD-B-D in 10 seconds is 93.23%, the removal rate reaches more than 99% in 1 minute, and the removal rate is close to 100% in 30 minutes (lower than the quantitative limit of an instrument). In contrast, GAC did not reach equilibrium within 30min with a removal of only 77.71%, whereas the imperforate EPI-CDP did not reach equilibrium within 30min with a lower removal of only 70.42%.

(2) 2-Naphthol (C)_s：0.76g L^-1)

PBCD-B-D on 2-naphthol at 2.4mmol L^-1The adsorption capacity at the initial concentration reaches 2.50mmol g^-1Much higher than GAC (1.52mmol g)^-1) And EPI-CDP (0.77mmol g)^-1). The removal rate of PBCD-B-D in 10 seconds is 95.99%, the removal rate reaches more than 99% in 1 minute, and the removal rate is close to 100% in 30 minutes (lower than the quantitative limit of an instrument). In contrast, GAC and EPI-CDP did not reach equilibrium within 30min, with removal rates of only 85.55% and 49.22%, respectively.

(3) P-nitrophenol (C)_s：11.6g L^-1)

PBCD-B-D adsorbing p-nitrophenol at 2.4mmol L^-1InitialThe adsorption capacity at the concentration reaches 1.96mmol g^-1Much higher than GAC (1.32mmol g)^-1) And EPI-CDP (0.43mmol g)^-1). The removal rate of PBCD-B-D in 10 seconds is 79.25%, the removal rate reaches more than 95% in 1 minute, and the removal rate is close to 100% in 30 minutes (lower than the quantitative limit of an instrument). In contrast, GAC and EPI-CDP did not reach equilibrium within 30min, with removal rates of only 87.74% and 47.34%, respectively.

(4) 4-chlorophenol (C)_s：24g L^-1)

PBCD-B-D p-4-chlorophenol in 2.4mmol L^-1The adsorption capacity at the initial concentration reaches 1.96mmol g^-1Much higher than GAC (0.99mmol g)^-1) And EPI-CDP (0.22mmol g)^-1). PBCD-B-D has a removal rate of 89.91% in 10 seconds, a removal rate of more than 95% in 1 minute, and a removal rate of nearly 100% in 30 minutes (below the quantitative limit of the instrument). In contrast, GAC and EPI-CDP did not reach equilibrium within 30min, with removal rates of only 74.49% and 29.01%, respectively. It can be seen that the high specific surface area is a key factor of adsorption capacity, while PBCD-B-D still has good adsorption performance for hydrophilic contaminants since it is more likely to hydrogen bond with hydrophilic contaminants due to the large number of surface hydroxyl groups retained on cyclodextrin. These results indicate that PBCD-B-D is an effective amphiphilic adsorbent.

Example 4:

regeneration experiments for the preparation of amphiphilic ultra-highly crosslinked porous cyclodextrin polymers PBCD-B-D prepared in example 1:

the specific method for the regeneration performance test of the material comprises the following steps: 40mg of PBCD-B-D was added to 40mL of 0.1mmol L^-1In 3-phenylphenol at 20 ℃ and 200rpm for 10 minutes. PBCD-B-D was isolated by filtration and regenerated by desorption with ethanol. The concentration of 3-phenylphenol in the filtrate was analyzed to calculate the removal efficiency. This process was repeated five times to study the regeneration performance.

PBCD-B-D can be rapidly adsorbed and desorbed by simple ethanol elution regeneration, as shown in FIG. 8. The 3-phenylphenol is subjected to 5 times of adsorption-desorption experiments at normal temperature, and the adsorption efficiency is not obviously reduced and still kept at 97.89%. Therefore, the porous cyclodextrin polymer is a material which can be used for adsorption and enrichment and has very excellent adsorption performance and good reproducibility

FIG. 1 is a synthesis scheme of a highly crosslinked porous cyclodextrin polymer PBCD-B-D. The beta-cyclodextrin is partially benzylated and then crosslinked with alkylating reagents biphenyl dichlorobenzyl and p-dichlorobenzyl to form the porous polymer.

FIG. 2 shows the change in contact angle of the polymer after adjustment of the benzylation ratio. When the benzylation ratio of beta-cyclodextrin is from 14:1 is reduced to 7: 1, the material changes from being superhydrophobic to hydrophilic on the surface due to the action of hydroxyl groups. The high-benzylation cyclodextrin material has poor wettability due to super-hydrophobicity and light weight, and affects the diffusion process of liquid phase adsorption. In contrast, PBCD-B-D disperses rapidly in water. This good wetting ability, combined with its porous structure, provides conditions for rapid removal of organic contaminants. We can use the material under different conditions by adjusting the degree of benzylation, for example in gas adsorption where water interference needs to be removed.

Figure 3 is a plot of the nitrogen adsorption isotherm and pore size distribution of PBCD-B-D in example 1 and example 2. It can be seen that the materials all exhibit ultra high specific surface areas and large micropore volumes. Meanwhile, the pore structure distribution is mainly micropores.

FIG. 4 is a thermogravimetric analysis and infrared spectrum of PBCD-B-D of example 1. As can be seen from the thermogravimetric curves, PBCD-B-D lost only 5% of its mass at 275 ℃. Compared with other cyclodextrin materials, the cyclodextrin material has higher crosslinking degree and higher thermal stability. The good thermal stability shows the advantage of the material in practical applications.

PBCD, beta-cyclodextrin, PBCD-B-D, DCX and BCMBP are sequentially arranged from top to bottom in the infrared spectrum. PBCD-B-D was found to be at 3400cm in wavelength compared to the infrared spectrum of beta-cyclodextrin^-1There was still a clear hydroxyl peak indicating that cyclodextrin hydroxyl groups were partially retained. 1450cm^-1To 1600cm^-1Signals in the range indicate aromatic ring formation, 680cm^-1To 880cm^-1The peak of (a) reflects the bending shock absorption of the aromatic ring to the hydrocarbon. 1100cm^-1The peak in (b) indicates the presence of fatty ethers. In addition, PBCD-B-D was found to be 680cm in comparison with the reaction starting materials biphenyl dichlorobenzyl and p-dichlorobenzyl^-1The chloromethyl peak disappeared, and these signals indicate crosslinking of the polymer.

FIG. 5 is a scanning electron microscope and a transmission electron microscope image of PBCD-B-D in example 1. The surface appearance and uniform particle size of PBCD-B-D can be seen from the SEM image. The material has an obvious macroporous structure, which is consistent with the pore size distribution obtained by nitrogen adsorption isotherm. As can be seen from the TEM image, the material has a large amount of micropore structures, and the material is proved to have large pore volume and ultrahigh specific surface area.