CN115449086A - A kind of amino-modified MIL-101 (Cr) and its preparation method and application - Google Patents
A kind of amino-modified MIL-101 (Cr) and its preparation method and application Download PDFInfo
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- 239000013178 MIL-101(Cr) Substances 0.000 title claims abstract description 84
- 238000002360 preparation method Methods 0.000 title claims abstract description 25
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims abstract description 37
- 239000013177 MIL-101 Substances 0.000 claims abstract description 34
- 125000002924 primary amino group Chemical group [H]N([H])* 0.000 claims abstract description 26
- 238000001179 sorption measurement Methods 0.000 claims abstract description 24
- 239000003607 modifier Substances 0.000 claims abstract description 19
- RPNUMPOLZDHAAY-UHFFFAOYSA-N Diethylenetriamine Chemical compound NCCNCCN RPNUMPOLZDHAAY-UHFFFAOYSA-N 0.000 claims abstract description 13
- 238000009849 vacuum degassing Methods 0.000 claims abstract description 9
- VILCJCGEZXAXTO-UHFFFAOYSA-N 2,2,2-tetramine Chemical compound NCCNCCNCCN VILCJCGEZXAXTO-UHFFFAOYSA-N 0.000 claims abstract description 6
- 238000002156 mixing Methods 0.000 claims abstract description 6
- 125000003916 ethylene diamine group Chemical group 0.000 claims abstract description 5
- 239000011148 porous material Substances 0.000 claims description 21
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims description 18
- PHFQLYPOURZARY-UHFFFAOYSA-N chromium trinitrate Chemical compound [Cr+3].[O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O PHFQLYPOURZARY-UHFFFAOYSA-N 0.000 claims description 12
- 238000001035 drying Methods 0.000 claims description 12
- 238000001027 hydrothermal synthesis Methods 0.000 claims description 12
- KKEYFWRCBNTPAC-UHFFFAOYSA-N Terephthalic acid Chemical compound OC(=O)C1=CC=C(C(O)=O)C=C1 KKEYFWRCBNTPAC-UHFFFAOYSA-N 0.000 claims description 10
- 229910002092 carbon dioxide Inorganic materials 0.000 claims description 9
- 238000005406 washing Methods 0.000 claims description 9
- 239000001569 carbon dioxide Substances 0.000 claims description 7
- 238000000034 method Methods 0.000 claims description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 7
- 238000001816 cooling Methods 0.000 claims description 5
- 239000007788 liquid Substances 0.000 claims description 4
- 238000000926 separation method Methods 0.000 claims description 4
- 239000003463 adsorbent Substances 0.000 claims description 3
- 239000011651 chromium Substances 0.000 claims description 2
- 239000000463 material Substances 0.000 abstract description 5
- 229910052751 metal Inorganic materials 0.000 abstract description 4
- 239000002184 metal Substances 0.000 abstract description 4
- 150000001875 compounds Chemical class 0.000 abstract description 2
- 239000013110 organic ligand Substances 0.000 abstract description 2
- 230000001737 promoting effect Effects 0.000 abstract 1
- 239000000047 product Substances 0.000 description 6
- 239000000203 mixture Substances 0.000 description 5
- 238000005119 centrifugation Methods 0.000 description 4
- ZMXDDKWLCZADIW-UHFFFAOYSA-N N,N-Dimethylformamide Chemical compound CN(C)C=O ZMXDDKWLCZADIW-UHFFFAOYSA-N 0.000 description 3
- 125000003277 amino group Chemical group 0.000 description 3
- 238000000967 suction filtration Methods 0.000 description 3
- 238000004438 BET method Methods 0.000 description 2
- ZHNUHDYFZUAESO-UHFFFAOYSA-N Formamide Chemical compound NC=O ZHNUHDYFZUAESO-UHFFFAOYSA-N 0.000 description 2
- 239000004809 Teflon Substances 0.000 description 2
- 229920006362 Teflon® Polymers 0.000 description 2
- 239000008367 deionised water Substances 0.000 description 2
- 229910021641 deionized water Inorganic materials 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 230000002378 acidificating effect Effects 0.000 description 1
- 238000002159 adsorption--desorption isotherm Methods 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 238000007872 degassing Methods 0.000 description 1
- 238000003795 desorption Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 239000012621 metal-organic framework Substances 0.000 description 1
- 238000000696 nitrogen adsorption--desorption isotherm Methods 0.000 description 1
- -1 polytetrafluoroethylene Polymers 0.000 description 1
- 229920001343 polytetrafluoroethylene Polymers 0.000 description 1
- 239000004810 polytetrafluoroethylene Substances 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
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Abstract
Description
技术领域technical field
本发明属于化合物的制备技术领域,具体涉及一种氨基改性MIL-101(Cr)及其制备方法和应用。The invention belongs to the technical field of compound preparation, and in particular relates to an amino-modified MIL-101 (Cr) and its preparation method and application.
背景技术Background technique
目前,金属有机框架材料由于其较大的表面积和孔道结构,因此,对有害气体具有良好的吸附性能。MIL-101(Cr)虽然也具有较大的比表面积和孔道结构,但是用作二氧化碳吸附材料时,其是通过二氧化碳气体分子和MIL-101(Cr)之间的范德华力相互作用完成吸附,由于这种结合力比较弱,被吸附的物质易发生解吸,导致二氧化碳吸附量比较小,吸附性能不佳。At present, metal organic framework materials have good adsorption properties for harmful gases due to their large surface area and pore structure. Although MIL-101(Cr) also has a large specific surface area and pore structure, when it is used as a carbon dioxide adsorption material, it completes the adsorption through the van der Waals interaction between carbon dioxide gas molecules and MIL-101(Cr). This binding force is relatively weak, and the adsorbed substances are prone to desorption, resulting in relatively small carbon dioxide adsorption capacity and poor adsorption performance.
发明内容Contents of the invention
有鉴于此,本发明的目的在于提供了一种氨基改性MIL-101(Cr)及其制备方法和应用,本发明所提供的制备方法制备得到的氨基改性MIL-101(Cr)对二氧化碳具有良好的吸附性能。In view of this, the object of the present invention is to provide a kind of amino-modified MIL-101 (Cr) and its preparation method and application, and the amino-modified MIL-101 (Cr) prepared by the preparation method provided by the present invention is to carbon dioxide Has good adsorption properties.
为了解决上述问题,本发明提供了一种氨基改性MIL-101(Cr)的制备方法,包括以下步骤:In order to solve the above problems, the invention provides a kind of preparation method of amino-modified MIL-101 (Cr), comprising the following steps:
将MIL-101(Cr)进行真空脱气,得到脱气后的MIL-101(Cr);Carry out vacuum degassing to MIL-101(Cr) to obtain degassed MIL-101(Cr);
将脱气后的MIL-101(Cr)和乙醇混合,所得MIL-101(Cr)的乙醇溶液和氨基改性剂混合,进行嫁接反应,得到氨基改性MIL-101(Cr);Mix the degassed MIL-101(Cr) with ethanol, mix the ethanol solution of the obtained MIL-101(Cr) with an amino modifier, and perform a grafting reaction to obtain amino-modified MIL-101(Cr);
所述氨基改性剂为乙二胺、二乙烯三胺或三乙烯四胺;The amino modifier is ethylenediamine, diethylenetriamine or triethylenetetramine;
所述MIL-101(Cr)和氨基改性剂的质量比为1:0.009~0.07。The mass ratio of the MIL-101 (Cr) to the amino modifier is 1:0.009-0.07.
优选地,所述嫁接反应的温度为100~130℃,时间为10~13h。Preferably, the temperature of the grafting reaction is 100-130° C., and the time is 10-13 hours.
优选地,所述真空脱气的温度为110~130℃,保温时间为10~15h,真空度为-0.01~0.09MPa。Preferably, the vacuum degassing temperature is 110-130° C., the holding time is 10-15 hours, and the vacuum degree is -0.01-0.09 MPa.
优选地,所述嫁接反应后,还包括将嫁接反应所得产物依次进行冷却、固液分离、洗涤和干燥。Preferably, after the grafting reaction, cooling, solid-liquid separation, washing and drying of the product obtained in the grafting reaction are further included.
优选地,所述干燥的温度为80℃。Preferably, the drying temperature is 80°C.
优选地,所述MIL-101(Cr)的制备方法,包括以下步骤:Preferably, the preparation method of the MIL-101 (Cr) comprises the following steps:
将硝酸铬、对苯二甲酸和水混合,进行水热反应,得到所述MIL-101材料。Chromium nitrate, terephthalic acid and water are mixed for hydrothermal reaction to obtain the MIL-101 material.
优选地,水热反应的温度为220℃,保温时间为8h。Preferably, the temperature of the hydrothermal reaction is 220° C., and the holding time is 8 hours.
本发明还提供了上述所述的制备方法制备得到的氨基改性MIL-101(Cr),所述氨基改性MIL-101(Cr)的比表面积为2800~3000m2/g,孔体积为0.7~1.4cm3/g,平均孔径为1.2~2.2nm。The present invention also provides the amino-modified MIL-101(Cr) prepared by the above-mentioned preparation method, the specific surface area of the amino-modified MIL-101(Cr) is 2800-3000m 2 /g, and the pore volume is 0.7 ~1.4cm 3 /g, and the average pore diameter is 1.2~2.2nm.
本发明还提供了上述所述的制备方法得到的氨基改性MIL-101(Cr)或上述所述的氨基改性MIL-101(Cr)在吸附二氧化碳中的应用。The present invention also provides the application of the amino-modified MIL-101(Cr) obtained by the above-mentioned preparation method or the above-mentioned amino-modified MIL-101(Cr) in the adsorption of carbon dioxide.
优选地,所述氨基改性MIL-101(Cr)对CO2的吸附容量为850~1050mg/g。Preferably, the CO 2 adsorption capacity of the amino-modified MIL-101(Cr) is 850-1050 mg/g.
本发明提供了一种氨基改性MIL-101(Cr)的制备方法,包括以下步骤:将MIL-101(Cr)进行真空脱气,得到脱气后的MIL-101(Cr);将脱气后的MIL-101(Cr)和乙醇混合,所得MIL-101(Cr)的乙醇溶液和氨基改性剂混合,进行嫁接反应,得到氨基改性MIL-101(Cr);所述氨基改性剂为乙二胺、二乙烯三胺或三乙烯四胺;所述MIL-101(Cr)和氨基改性剂的质量比为1:0.009~0.07。本发明采用末端胺基的有机配体作为氨基改性剂,通过将氨基改性剂滴加至MIL-101(Cr)的乙醇溶液中进行嫁接反应,使氨基改性剂进入或者附着在MIL-101(Cr)的孔道或者表面,不占据不饱和金属位点,因此,在金属位点对CO2吸附的基础上增加了氨基对CO2的吸附,氨基属于碱性基团,而CO2属于酸性氧化物,吸附过程属于化学吸附,因此改性后的MIL-101(Cr)吸附CO2后,不易发生解吸,从而增加了CO2的吸附量。The invention provides a preparation method of amino-modified MIL-101(Cr), comprising the following steps: vacuum degassing MIL-101(Cr) to obtain degassed MIL-101(Cr); degassing The final MIL-101 (Cr) is mixed with ethanol, and the ethanol solution of the gained MIL-101 (Cr) is mixed with an amino modifier to carry out a grafting reaction to obtain an amino modified MIL-101 (Cr); the amino modifier It is ethylenediamine, diethylenetriamine or triethylenetetramine; the mass ratio of the MIL-101(Cr) to the amino modifier is 1:0.009-0.07. The present invention uses the organic ligand of the terminal amino group as the amino modifier, and the amino modifier is added dropwise to the ethanol solution of MIL-101 (Cr) to carry out the grafting reaction, so that the amino modifier enters or attaches to the MIL- The pores or surfaces of 101(Cr) do not occupy unsaturated metal sites. Therefore, the adsorption of amino groups to CO 2 is added on the basis of the adsorption of CO 2 on metal sites. Amino groups belong to basic groups, while CO 2 belongs to For acidic oxides, the adsorption process belongs to chemical adsorption, so after the modified MIL-101(Cr) adsorbs CO2 , it is not easy to desorb, thus increasing the amount of CO2 adsorbed.
附图说明Description of drawings
图1为实施例1制备得到的DETA改性的MIL-101(Cr)采用BET法测试得到的N2吸脱附等温线图;Fig. 1 adopts the N that the DETA modified MIL-101 (Cr) that embodiment 1 prepares adopts BET method to test and obtain The adsorption - desorption isotherm figure;
图2为实施例1制备得到的DETA改性的MIL-101(Cr)对CO2的吸附测试图;Fig. 2 is the DETA modified MIL-101 (Cr) that embodiment 1 prepares to CO The adsorption test figure;
图3为实施例1~3中0.03-DETA-MIL-101、0.03-EDA-MIL-101和0.03-EDA-MIL-101对CO2的吸附测试图。Fig. 3 is the adsorption test graph of 0.03-DETA-MIL-101, 0.03-EDA-MIL-101 and 0.03-EDA-MIL-101 for CO 2 in Examples 1-3.
具体实施方式detailed description
本发明提供了一种氨基改性MIL-101(Cr)的制备方法,包括以下步骤:The invention provides a kind of preparation method of amino-modified MIL-101 (Cr), comprising the following steps:
将MIL-101(Cr)进行真空脱气,得到脱气后的MIL-101(Cr);Carry out vacuum degassing to MIL-101(Cr) to obtain degassed MIL-101(Cr);
将脱气后的MIL-101(Cr)和乙醇混合,所得MIL-101(Cr)的乙醇溶液和氨基改性剂混合,进行嫁接反应,得到氨基改性MIL-101(Cr)。The degassed MIL-101(Cr) is mixed with ethanol, the ethanol solution of the obtained MIL-101(Cr) is mixed with an amino modifier, and a grafting reaction is carried out to obtain the amino-modified MIL-101(Cr).
本发明将MIL-101(Cr)进行真空脱气,得到脱气后的MIL-101(Cr)。In the present invention, the MIL-101 (Cr) is subjected to vacuum degassing to obtain the degassed MIL-101 (Cr).
在本发明中,所述MIL-101(Cr)的制备方法优选包括以下步骤:In the present invention, the preparation method of the MIL-101(Cr) preferably comprises the following steps:
将硝酸铬、对苯二甲酸和水混合,进行水热反应,得到所述MIL-101材料。Chromium nitrate, terephthalic acid and water are mixed for hydrothermal reaction to obtain the MIL-101 material.
在本发明中,所述水优选为去离子水;所述硝酸铬和对苯二甲酸的质量比优选为1:0.415;所述硝酸铬和水的质量比优选为1:12~15,更优选为1:13~14。In the present invention, the water is preferably deionized water; the mass ratio of the chromium nitrate and terephthalic acid is preferably 1:0.415; the mass ratio of the chromium nitrate and water is preferably 1:12~15, more preferably Preferably it is 1:13-14.
在本发明中,所述水热反应的温度优选为220℃;所述水热反应的保温时间优选为8h。In the present invention, the temperature of the hydrothermal reaction is preferably 220° C.; the holding time of the hydrothermal reaction is preferably 8 hours.
在本发明中,所述水热反应后,优选还包括将水热反应所得产物依次进行抽滤、洗涤和干燥。In the present invention, after the hydrothermal reaction, it is preferred to further include suction filtration, washing and drying of the product obtained from the hydrothermal reaction in sequence.
在本发明中,对所述抽滤不作具体限定,采用本领域技术人员熟知的抽滤操作得到水热反应产物即可。在本发明中,所述洗涤优选为依次进行N,N-二甲基甲酰胺洗涤和无水乙醇洗涤。在本发明中,所述干燥的温度优选为80℃,时间为12h。In the present invention, the suction filtration is not specifically limited, and the hydrothermal reaction product can be obtained by the suction filtration operation well known to those skilled in the art. In the present invention, the washing is preferably performed sequentially with N,N-dimethylformamide washing and absolute ethanol washing. In the present invention, the drying temperature is preferably 80° C. and the drying time is 12 hours.
在本发明中,所述真空脱气的温度优选为110~130℃,更优选为120℃,保温时间优选为10~15h,更优选为11~12h;真空度优选为-0.10~0.09MPa,更优选为0MPa。In the present invention, the temperature of the vacuum degassing is preferably 110-130°C, more preferably 120°C, the holding time is preferably 10-15h, more preferably 11-12h; the degree of vacuum is preferably -0.10-0.09MPa, More preferably, it is 0 MPa.
得到脱气后的MIL-101(Cr)后,本发明将脱气后的MIL-101(Cr)和乙醇混合,所得MIL-101(Cr)的乙醇溶液和氨基改性剂混合,进行嫁接反应,得到氨基改性MIL-101(Cr)。After the degassed MIL-101 (Cr) is obtained, the present invention mixes the degassed MIL-101 (Cr) with ethanol, mixes the ethanol solution of the obtained MIL-101 (Cr) with an amino modifier, and performs grafting reaction , to obtain amino-modified MIL-101 (Cr).
在本发明中,所述氨基改性剂为乙二胺、二乙烯三胺或三乙烯四胺。在本发明中,所述MIL-101(Cr)的乙醇溶液中MIL-101(Cr)的质量分数优选为1.5~2.5%,更优选为1.9~2.3%。在本发明中,所述MIL-101(Cr)的质量和氨基改性剂的质量比优选为1:0.009~0.07,更优选为1:0.04~0.06。In the present invention, the amino modifier is ethylenediamine, diethylenetriamine or triethylenetetramine. In the present invention, the mass fraction of MIL-101(Cr) in the ethanol solution of MIL-101(Cr) is preferably 1.5-2.5%, more preferably 1.9-2.3%. In the present invention, the mass ratio of the MIL-101 (Cr) to the amino modifier is preferably 1:0.009-0.07, more preferably 1:0.04-0.06.
在本发明中,所述混合优选为将所述氨基改性剂滴加至MIL-101(Cr)的乙醇溶液中。In the present invention, the mixing is preferably adding the amino modifier dropwise into the ethanol solution of MIL-101(Cr).
在本发明中,所述嫁接反应的温度优选为100~130℃,更优选为120℃,时间优选为10~13h,更优选为12h。在本发明中,所述嫁接反应后,还包括将嫁接反应所得产物依次进行冷却、固液分离、洗涤和干燥。In the present invention, the temperature of the grafting reaction is preferably 100-130° C., more preferably 120° C., and the time is preferably 10-13 hours, more preferably 12 hours. In the present invention, after the grafting reaction, cooling, solid-liquid separation, washing and drying of the product obtained in the grafting reaction are also included.
在本发明中,所述冷却优选冷却至室温,对所述冷却的方式不作具体限定。在本发明中,所述固液分离的方式为离心,所述离心的转速优选为4000~7000rpm,更优选为5000rpm。所述离心的时间优选为3min。在本发明中,所述洗涤的试剂优选为乙醇,所述洗涤的次数优选为3次。在本发明中,所述干燥的温度优选为100~110℃,更优选为105℃,所述干燥的时间优选为12h。In the present invention, the cooling is preferably to room temperature, and the cooling method is not specifically limited. In the present invention, the solid-liquid separation method is centrifugation, and the rotational speed of the centrifugation is preferably 4000-7000 rpm, more preferably 5000 rpm. The centrifugation time is preferably 3 minutes. In the present invention, the washing reagent is preferably ethanol, and the washing times are preferably 3 times. In the present invention, the drying temperature is preferably 100-110° C., more preferably 105° C., and the drying time is preferably 12 hours.
本发明还提供了上述所述制备方法制备得到的氨基改性MIL-101(Cr),所述氨基改性MIL-101(Cr)的比表面积优选为2800~3000m2/g,更优选为2900m2/g;所述氨基改性MIL-101(Cr)的孔体积优选为0.7~1.4cm3/g,更优选为1.0~1.3cm3/g,孔径优选为1.2~2.2nm,更优选为1.5~2.0nm。The present invention also provides the amino-modified MIL-101(Cr) prepared by the above-mentioned preparation method, the specific surface area of the amino-modified MIL-101(Cr) is preferably 2800-3000m 2 /g, more preferably 2900m2/g 2 /g; the pore volume of the amino-modified MIL-101(Cr) is preferably 0.7-1.4 cm 3 /g, more preferably 1.0-1.3 cm 3 /g, and the pore diameter is preferably 1.2-2.2 nm, more preferably 1.5-2.0nm.
本发明还提供了上述所述的制备方法制备得到的氨基改性MIL-101(Cr)在吸附二氧化碳中的应用。The present invention also provides the application of the amino-modified MIL-101(Cr) prepared by the above-mentioned preparation method in absorbing carbon dioxide.
在本发明中,所述氨基改性MIL-101(Cr)对CO2的吸附容量优选为850~1050mg/g,更优选为900~1040mg/g。In the present invention, the CO 2 adsorption capacity of the amino-modified MIL-101(Cr) is preferably 850-1050 mg/g, more preferably 900-1040 mg/g.
为了进一步说明本发明,下面结合实施例对本发明提供的技术方案进行详细叙述,但不能将它们理解为对本发明保护范围的限定。In order to further illustrate the present invention, the technical solutions provided by the present invention are described in detail below in conjunction with the examples, but they cannot be interpreted as limiting the protection scope of the present invention.
实施例1Example 1
MIL-101(Cr)的制备:Preparation of MIL-101(Cr):
将4g硝酸铬,1.66g对苯二甲酸,48g去离子水混合,室温超声20min,搅拌1h混匀后,倒入聚四氟乙烯内衬中,再将内衬放在防爆的特氟龙高压釜中,放在烘箱中,在220℃的条温度下水热反应8h,反应结束后,待高压釜自然冷却至室温,然后将水热反应所得产物离心离心所得沉淀物,用氮氮二甲基甲酰胺和无水乙醇多次洗涤后进行干燥(干燥的温度为80℃,时间为12h),得到所述MIL-101(Cr)。Mix 4g of chromium nitrate, 1.66g of terephthalic acid, and 48g of deionized water, ultrasonicate at room temperature for 20 minutes, stir for 1 hour and mix well, then pour it into the Teflon lining, and then put the lining on an explosion-proof Teflon high pressure Put it in an oven, and conduct a hydrothermal reaction at a temperature of 220°C for 8 hours. After the reaction, wait for the autoclave to cool down to room temperature naturally, and then centrifuge the product obtained from the hydrothermal reaction to obtain a precipitate. The MIL-101(Cr) was obtained after being washed with formamide and absolute ethanol several times and then dried (the drying temperature was 80° C. and the drying time was 12 h).
氨基改性MIL-101(Cr)的制备:Preparation of amino-modified MIL-101(Cr):
将0.5gMIL-101(Cr)在120℃的真空烘箱中真空脱气12h,得到脱气后的MIL-101(Cr),将脱气后的MIL-101(Cr)与30mL无水乙醇混合,然后用移液枪分别滴加0.01、0.03、0.05、0.07mL的DETA,搅拌10min,然后将混合液移入到内村为聚四氟乙烯的100mL反应釜中。之后密封反应釜,放入到温度为100℃恒温鼓风烘箱中嫁接反应12h。嫁接反应后,将嫁接反应所得产物依次进行冷却(冷却至室温)、离心(转速为4000rpm,时间为3min),离心所得产物用乙醇洗涤3次后放入真空烘箱100℃干燥12h,即为DETA改性的MIL-101(Cr),记为0.01-DETA-MIL-101、0.03-DETA-MIL-101、0.05-DETA-MIL-101和0.07-DETA-MIL-101。0.5g MIL-101(Cr) was vacuum degassed in a vacuum oven at 120°C for 12h to obtain the degassed MIL-101(Cr), and the degassed MIL-101(Cr) was mixed with 30mL of absolute ethanol, Then use a pipette gun to add 0.01, 0.03, 0.05, and 0.07 mL of DETA dropwise, stir for 10 min, and then transfer the mixture into a 100 mL reaction kettle with polytetrafluoroethylene as the inner wall. Afterwards, the reaction kettle was sealed, and put into a constant temperature blast oven at 100°C for grafting reaction for 12 hours. After the grafting reaction, the product obtained from the grafting reaction is cooled (cooled to room temperature) and centrifuged (rotating speed is 4000rpm, time is 3min), and the product obtained by centrifugation is washed with ethanol for 3 times and then put into a vacuum oven for 12 hours at 100°C to dry, which is DETA Modified MIL-101 (Cr), denoted as 0.01-DETA-MIL-101, 0.03-DETA-MIL-101, 0.05-DETA-MIL-101 and 0.07-DETA-MIL-101.
实施例2Example 2
与实施例1中“氨基改性MIL-101(Cr)的制备”的区别仅仅在于将DETA替换为EDA,得到0.01-EDA-MIL-101、0.03-EDA-MIL-101、0.05-EDA-MIL-101和0.07-EDA-MIL-101。The difference from the "preparation of amino-modified MIL-101 (Cr)" in Example 1 is only that DETA is replaced by EDA to obtain 0.01-EDA-MIL-101, 0.03-EDA-MIL-101, 0.05-EDA-MIL -101 and 0.07-EDA-MIL-101.
实施例3Example 3
与实施例1中“氨基改性MIL-101(Cr)的制备”的区别仅仅在于将DETA替换为TETA,得到0.01-TETA-MIL-101、0.03-TETA-MIL-101、0.05-TETA-MIL-101和0.07-TETA-MIL-101。The difference from the "preparation of amino-modified MIL-101 (Cr)" in Example 1 is only that DETA is replaced by TETA to obtain 0.01-TETA-MIL-101, 0.03-TETA-MIL-101, 0.05-TETA-MIL -101 and 0.07-TETA-MIL-101.
本发明对实施例1制备得到的DETA改性的MIL-101(Cr)采用BET法测试,得到N2吸脱附等温线图,见图1。根据图1,计算可得DETA改性的MIL-101(Cr)的比表面积、孔体积和平均孔径,结果见表1。The present invention uses the BET method to test the DETA-modified MIL-101 (Cr) prepared in Example 1, and obtains the N2 adsorption-desorption isotherm diagram, see FIG. 1 . According to Figure 1, the specific surface area, pore volume and average pore diameter of DETA-modified MIL-101 (Cr) can be calculated, and the results are shown in Table 1.
表1 DETA改性的MIL-101(Cr)的比表面积、孔体积和平均孔径Table 1 Specific surface area, pore volume and average pore diameter of DETA modified MIL-101(Cr)
本发明对实施例1制备得到的DETA改性的MIL-101(Cr)对CO2的吸附进行了测试,测试结果见图2,从图2可知,未改性MIL-101(Cr)的CO2吸附量为850mg/g,当DETA添加量为0.03mL时CO2吸附量提高的最大为980mg/g,吸附量提高了15.3%。The present invention tests the DETA-modified MIL-101 (Cr) prepared in Example 1 to the adsorption of CO 2 , and the test results are shown in Fig. 2. As can be seen from Fig. 2, the CO 2 The adsorption capacity is 850mg/g, and when the amount of DETA added is 0.03mL, the CO 2 adsorption capacity increases to a maximum of 980 mg/g, and the adsorption capacity increases by 15.3%.
本发明对实施例1~3中0.03-DETA-MIL-101、0.03-EDA-MIL-101和0.03-EDA-MIL-101对CO2的吸附进行了测试,测试结果见图3,从图3可知:EDA添加量为0.03mL时CO2吸附量提高的最大为1045mg/g,吸附量较未改性的MIL-101(Cr)提高了23%。根据图3,计算可得0.03-DETA-MIL-101、0.03-EDA-MIL-101和0.03-EDA-MIL-101的比表面积、孔体积和平均孔径,结果见表2。The present invention tests the adsorption of CO by 0.03-DETA-MIL-101, 0.03-EDA-MIL-101 and 0.03-EDA-MIL-101 in Examples 1 to 3, and the test results are shown in Fig. 3, from Fig. 3 It can be seen that when the amount of EDA added is 0.03mL, the CO 2 adsorption capacity increases up to 1045 mg/g, which is 23% higher than that of the unmodified MIL-101(Cr). According to Figure 3, the specific surface area, pore volume and average pore diameter of 0.03-DETA-MIL-101, 0.03-EDA-MIL-101 and 0.03-EDA-MIL-101 can be calculated, and the results are shown in Table 2.
表2 0.03-DETA-MIL-101、0.03-EDA-MIL-101和0.03-EDA-MIL-101的比表面积、孔体积和平均孔径Table 2 Specific surface area, pore volume and average pore diameter of 0.03-DETA-MIL-101, 0.03-EDA-MIL-101 and 0.03-EDA-MIL-101
以上所述仅是本发明的优选实施方式,应当指出,对于本技术领域的普通技术人员来说,在不脱离本发明原理的前提下,还可以做出若干改进和润视,这些改进和润饰也应视为本发明的保护范围。The above is only a preferred embodiment of the present invention, and it should be pointed out that for those of ordinary skill in the art, without departing from the principle of the present invention, some improvements and embellishments can also be made. These improvements and embellishments It should also be regarded as the protection scope of the present invention.
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