CN114904587B - Preparation method of cesium modified phosphotungstic acid@UiO-66/porous carbon-based composite material - Google Patents
Preparation method of cesium modified phosphotungstic acid@UiO-66/porous carbon-based composite material Download PDFInfo
- Publication number
- CN114904587B CN114904587B CN202210579623.3A CN202210579623A CN114904587B CN 114904587 B CN114904587 B CN 114904587B CN 202210579623 A CN202210579623 A CN 202210579623A CN 114904587 B CN114904587 B CN 114904587B
- Authority
- CN
- China
- Prior art keywords
- uio
- porous carbon
- cesium
- phosphotungstic acid
- composite material
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 title claims abstract description 21
- 229910052799 carbon Inorganic materials 0.000 title claims abstract description 21
- 239000002131 composite material Substances 0.000 title claims abstract description 21
- 238000002360 preparation method Methods 0.000 title claims abstract description 16
- 229910052792 caesium Inorganic materials 0.000 title 1
- -1 cesium modified phosphotungstic acid Chemical class 0.000 title 1
- 239000002028 Biomass Substances 0.000 claims abstract description 36
- 239000003575 carbonaceous material Substances 0.000 claims abstract description 32
- IYDGMDWEHDFVQI-UHFFFAOYSA-N phosphoric acid;trioxotungsten Chemical class O=[W](=O)=O.O=[W](=O)=O.O=[W](=O)=O.O=[W](=O)=O.O=[W](=O)=O.O=[W](=O)=O.O=[W](=O)=O.O=[W](=O)=O.O=[W](=O)=O.O=[W](=O)=O.O=[W](=O)=O.O=[W](=O)=O.OP(O)(O)=O IYDGMDWEHDFVQI-UHFFFAOYSA-N 0.000 claims abstract description 22
- 238000006243 chemical reaction Methods 0.000 claims abstract description 16
- 239000001913 cellulose Substances 0.000 claims abstract description 13
- 229920002678 cellulose Polymers 0.000 claims abstract description 13
- 239000002994 raw material Substances 0.000 claims abstract description 13
- 239000011148 porous material Substances 0.000 claims abstract description 4
- ZMXDDKWLCZADIW-UHFFFAOYSA-N N,N-Dimethylformamide Chemical compound CN(C)C=O ZMXDDKWLCZADIW-UHFFFAOYSA-N 0.000 claims description 18
- 238000003756 stirring Methods 0.000 claims description 17
- 239000000243 solution Substances 0.000 claims description 15
- KKEYFWRCBNTPAC-UHFFFAOYSA-N Terephthalic acid Chemical compound OC(=O)C1=CC=C(C(O)=O)C=C1 KKEYFWRCBNTPAC-UHFFFAOYSA-N 0.000 claims description 12
- BDAGIHXWWSANSR-UHFFFAOYSA-N methanoic acid Natural products OC=O BDAGIHXWWSANSR-UHFFFAOYSA-N 0.000 claims description 12
- 239000002243 precursor Substances 0.000 claims description 11
- 239000003795 chemical substances by application Substances 0.000 claims description 9
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 8
- 238000009835 boiling Methods 0.000 claims description 8
- 239000000203 mixture Substances 0.000 claims description 8
- TVFDJXOCXUVLDH-UHFFFAOYSA-N caesium atom Chemical class [Cs] TVFDJXOCXUVLDH-UHFFFAOYSA-N 0.000 claims description 7
- 238000006297 dehydration reaction Methods 0.000 claims description 7
- 229910052751 metal Inorganic materials 0.000 claims description 7
- 239000002184 metal Substances 0.000 claims description 7
- 150000003839 salts Chemical class 0.000 claims description 7
- OSWFIVFLDKOXQC-UHFFFAOYSA-N 4-(3-methoxyphenyl)aniline Chemical compound COC1=CC=CC(C=2C=CC(N)=CC=2)=C1 OSWFIVFLDKOXQC-UHFFFAOYSA-N 0.000 claims description 6
- NLSCHDZTHVNDCP-UHFFFAOYSA-N caesium nitrate Chemical compound [Cs+].[O-][N+]([O-])=O NLSCHDZTHVNDCP-UHFFFAOYSA-N 0.000 claims description 6
- 235000019253 formic acid Nutrition 0.000 claims description 6
- 239000011259 mixed solution Substances 0.000 claims description 6
- 229910021642 ultra pure water Inorganic materials 0.000 claims description 6
- 239000012498 ultrapure water Substances 0.000 claims description 6
- 241000219000 Populus Species 0.000 claims description 5
- 239000012266 salt solution Substances 0.000 claims description 5
- 239000012299 nitrogen atmosphere Substances 0.000 claims description 4
- 238000010992 reflux Methods 0.000 claims description 4
- WHMDKBIGKVEYHS-IYEMJOQQSA-L Zinc gluconate Chemical compound [Zn+2].OC[C@@H](O)[C@@H](O)[C@H](O)[C@@H](O)C([O-])=O.OC[C@@H](O)[C@@H](O)[C@H](O)[C@@H](O)C([O-])=O WHMDKBIGKVEYHS-IYEMJOQQSA-L 0.000 claims description 3
- PDPJQWYGJJBYLF-UHFFFAOYSA-J hafnium tetrachloride Chemical compound Cl[Hf](Cl)(Cl)Cl PDPJQWYGJJBYLF-UHFFFAOYSA-J 0.000 claims description 3
- 239000011670 zinc gluconate Substances 0.000 claims description 3
- 229960000306 zinc gluconate Drugs 0.000 claims description 3
- 235000011478 zinc gluconate Nutrition 0.000 claims description 3
- 235000017166 Bambusa arundinacea Nutrition 0.000 claims description 2
- 235000017491 Bambusa tulda Nutrition 0.000 claims description 2
- 235000010469 Glycine max Nutrition 0.000 claims description 2
- 244000068988 Glycine max Species 0.000 claims description 2
- 244000082204 Phyllostachys viridis Species 0.000 claims description 2
- 235000015334 Phyllostachys viridis Nutrition 0.000 claims description 2
- ZOIORXHNWRGPMV-UHFFFAOYSA-N acetic acid;zinc Chemical compound [Zn].CC(O)=O.CC(O)=O ZOIORXHNWRGPMV-UHFFFAOYSA-N 0.000 claims description 2
- 239000011425 bamboo Substances 0.000 claims description 2
- ZOAIGCHJWKDIPJ-UHFFFAOYSA-M caesium acetate Chemical compound [Cs+].CC([O-])=O ZOAIGCHJWKDIPJ-UHFFFAOYSA-M 0.000 claims description 2
- FJDQFPXHSGXQBY-UHFFFAOYSA-L caesium carbonate Chemical compound [Cs+].[Cs+].[O-]C([O-])=O FJDQFPXHSGXQBY-UHFFFAOYSA-L 0.000 claims description 2
- 229910000024 caesium carbonate Inorganic materials 0.000 claims description 2
- VYLVYHXQOHJDJL-UHFFFAOYSA-K cerium trichloride Chemical compound Cl[Ce](Cl)Cl VYLVYHXQOHJDJL-UHFFFAOYSA-K 0.000 claims description 2
- 235000013399 edible fruits Nutrition 0.000 claims description 2
- 239000010902 straw Substances 0.000 claims description 2
- 239000004246 zinc acetate Substances 0.000 claims description 2
- ZPEJZWGMHAKWNL-UHFFFAOYSA-L zinc;oxalate Chemical compound [Zn+2].[O-]C(=O)C([O-])=O ZPEJZWGMHAKWNL-UHFFFAOYSA-L 0.000 claims description 2
- NHXVNEDMKGDNPR-UHFFFAOYSA-N zinc;pentane-2,4-dione Chemical compound [Zn+2].CC(=O)[CH-]C(C)=O.CC(=O)[CH-]C(C)=O NHXVNEDMKGDNPR-UHFFFAOYSA-N 0.000 claims description 2
- DUNKXUFBGCUVQW-UHFFFAOYSA-J zirconium tetrachloride Chemical compound Cl[Zr](Cl)(Cl)Cl DUNKXUFBGCUVQW-UHFFFAOYSA-J 0.000 claims description 2
- 239000000969 carrier Substances 0.000 claims 1
- NOEGNKMFWQHSLB-UHFFFAOYSA-N 5-hydroxymethylfurfural Chemical compound OCC1=CC=C(C=O)O1 NOEGNKMFWQHSLB-UHFFFAOYSA-N 0.000 abstract description 12
- 239000003054 catalyst Substances 0.000 abstract description 12
- RJGBSYZFOCAGQY-UHFFFAOYSA-N hydroxymethylfurfural Natural products COC1=CC=C(C=O)O1 RJGBSYZFOCAGQY-UHFFFAOYSA-N 0.000 abstract description 12
- 238000000034 method Methods 0.000 abstract description 10
- 230000015572 biosynthetic process Effects 0.000 abstract description 3
- 238000009776 industrial production Methods 0.000 abstract description 3
- 238000003786 synthesis reaction Methods 0.000 abstract description 3
- 230000007613 environmental effect Effects 0.000 abstract description 2
- HYBBIBNJHNGZAN-UHFFFAOYSA-N furfural Chemical compound O=CC1=CC=CO1 HYBBIBNJHNGZAN-UHFFFAOYSA-N 0.000 abstract 2
- 238000011084 recovery Methods 0.000 abstract 1
- 230000003197 catalytic effect Effects 0.000 description 7
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical compound C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 description 6
- 230000018044 dehydration Effects 0.000 description 5
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical class C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 5
- 238000010438 heat treatment Methods 0.000 description 3
- 238000002390 rotary evaporation Methods 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 229930091371 Fructose Natural products 0.000 description 2
- RFSUNEUAIZKAJO-ARQDHWQXSA-N Fructose Chemical compound OC[C@H]1O[C@](O)(CO)[C@@H](O)[C@@H]1O RFSUNEUAIZKAJO-ARQDHWQXSA-N 0.000 description 2
- 239000005715 Fructose Substances 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 2
- 229910001430 chromium ion Inorganic materials 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 230000035484 reaction time Effects 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- 239000011973 solid acid Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 239000002253 acid Substances 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000002051 biphasic effect Effects 0.000 description 1
- 238000001354 calcination Methods 0.000 description 1
- 125000003178 carboxy group Chemical group [H]OC(*)=O 0.000 description 1
- 238000006555 catalytic reaction Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 239000012153 distilled water Substances 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 238000001027 hydrothermal synthesis Methods 0.000 description 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 230000001681 protective effect Effects 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- BDHFUVZGWQCTTF-UHFFFAOYSA-M sulfonate Chemical compound [O-]S(=O)=O BDHFUVZGWQCTTF-UHFFFAOYSA-M 0.000 description 1
- 238000006277 sulfonation reaction Methods 0.000 description 1
- YLQBMQCUIZJEEH-UHFFFAOYSA-N tetrahydrofuran Natural products C=1C=COC=1 YLQBMQCUIZJEEH-UHFFFAOYSA-N 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J31/00—Catalysts comprising hydrides, coordination complexes or organic compounds
- B01J31/26—Catalysts comprising hydrides, coordination complexes or organic compounds containing in addition, inorganic metal compounds not provided for in groups B01J31/02 - B01J31/24
- B01J31/34—Catalysts comprising hydrides, coordination complexes or organic compounds containing in addition, inorganic metal compounds not provided for in groups B01J31/02 - B01J31/24 of chromium, molybdenum or tungsten
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/50—Catalysts, in general, characterised by their form or physical properties characterised by their shape or configuration
- B01J35/56—Foraminous structures having flow-through passages or channels, e.g. grids or three-dimensional monoliths
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D307/00—Heterocyclic compounds containing five-membered rings having one oxygen atom as the only ring hetero atom
- C07D307/02—Heterocyclic compounds containing five-membered rings having one oxygen atom as the only ring hetero atom not condensed with other rings
- C07D307/34—Heterocyclic compounds containing five-membered rings having one oxygen atom as the only ring hetero atom not condensed with other rings having two or three double bonds between ring members or between ring members and non-ring members
- C07D307/38—Heterocyclic compounds containing five-membered rings having one oxygen atom as the only ring hetero atom not condensed with other rings having two or three double bonds between ring members or between ring members and non-ring members with substituted hydrocarbon radicals attached to ring carbon atoms
- C07D307/40—Radicals substituted by oxygen atoms
- C07D307/46—Doubly bound oxygen atoms, or two oxygen atoms singly bound to the same carbon atom
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Inorganic Chemistry (AREA)
- Catalysts (AREA)
- Furan Compounds (AREA)
- Carbon And Carbon Compounds (AREA)
Abstract
Description
技术领域Technical field
本发明属于生物质资源化利用领域,涉及一种铯改性的磷钨酸@UiO-66/多孔碳基复合材料的制备方法,具体的,是涉及一种CsxH3-xPW12O40@UiO-66/生物质多孔碳基复合材料的制备方法及其在纤维素脱水中的应用。The invention belongs to the field of biomass resource utilization and relates to a preparation method of cesium-modified phosphotungstic acid @UiO-66/porous carbon-based composite material. Specifically, it relates to a Cs x H 3-x PW 12 O 40 Preparation method of @UiO-66/biomass porous carbon-based composite materials and its application in cellulose dehydration.
背景技术Background technique
现有技术中,社会经济和科技的发展进步高度依赖于传统的化石资源,这些不可再生资源的储量随着人类需求的增加而日益消耗。因此,通过可再生能源代替不可再生能源是实现可持续发展的关键举措之一。纤维素作为自然界中储量丰富、来源广泛,价格低廉的可再生资源,具有清洁环保无污染的特点而受到广泛关注,将其催化转化为高附加值的化工产品被认为是一种具有吸引力和发展潜力的生物质利用方式。在众多的生物质基衍生品中,5-羟甲基糠醛(5-HMF)作为一种重要的平台化合物,具有较高经济利用价值,通常应用在医药,石油化工等领域。In the existing technology, the development and progress of social economy and science and technology are highly dependent on traditional fossil resources, and the reserves of these non-renewable resources are increasingly consumed as human needs increase. Therefore, replacing non-renewable energy with renewable energy is one of the key measures to achieve sustainable development. As a renewable resource with abundant reserves, wide sources, and low price in nature, cellulose has attracted widespread attention because of its clean, environmentally friendly and pollution-free characteristics. Its catalytic conversion into high value-added chemical products is considered an attractive and Development potential of biomass utilization. Among numerous biomass-based derivatives, 5-hydroxymethylfurfural (5-HMF), as an important platform compound, has high economic value and is usually used in medicine, petrochemical and other fields.
以纤维素作为原料制备5-HMF主要通过化学催化法,催化剂需要同时具有酸催化位点和碱催化位点,因此对催化的设计具有较高要求。专利CN103028424A公开一种用于5-羟甲基糠醛合成的固体酸催化剂的制备方法,所述的固体酸催化剂为氧化物负载硫酸根离子或铬离子,将其用于合成5-羟甲基糠醛中可获得较高的收率。催化剂的主要活性组分是硫酸根粒子和铬离子,在一定程度上会对环境造成负担。专利CN 109749738 A公开了一种磺化碳量子点在制备5羟甲基糠醛中的应用,以生物质为原料首先利用H2O2辅助的水热法制备表面含有羟基和羧基的碳量子点,然后对碳量子点进行磺化处理,最终获得磺化碳量子点。磺化碳量子点可作为催化剂用于催化果糖脱水生成5-羟甲基糠醛,具有高的果糖转化活性以及良好的5-HMF产率和优异的稳定性,然而催化剂制备过程的需要磺化,对环境产生一定的污染。Using cellulose as raw material to prepare 5-HMF is mainly through chemical catalysis. The catalyst needs to have both acid catalytic sites and alkali catalytic sites, so there are high requirements for catalytic design. Patent CN103028424A discloses a preparation method of a solid acid catalyst for the synthesis of 5-hydroxymethylfurfural. The solid acid catalyst is an oxide-loaded sulfate ion or chromium ion, which is used to synthesize 5-hydroxymethylfurfural. A higher yield can be obtained. The main active components of the catalyst are sulfate particles and chromium ions, which will burden the environment to a certain extent. Patent CN 109749738 A discloses the application of sulfonated carbon quantum dots in the preparation of 5-hydroxymethylfurfural. Using biomass as raw material, carbon quantum dots containing hydroxyl and carboxyl groups on the surface are first prepared using a hydrothermal method assisted by H 2 O 2 , and then sulfonate the carbon quantum dots to finally obtain sulfonated carbon quantum dots. Sulfonated carbon quantum dots can be used as catalysts to catalyze the dehydration of fructose to produce 5-hydroxymethylfurfural. They have high fructose conversion activity, good 5-HMF yield and excellent stability. However, the catalyst preparation process requires sulfonation. It will cause certain pollution to the environment.
发明内容Contents of the invention
针对上述问题,本发明提供了一种铯改性的磷钨酸@UiO-66/多孔碳基复合材料的制备方法及其在纤维素脱水中的应用;本发明提供的催化剂催化性能高效,合成工艺简单,回收方式简便,重复使用性能优异,原料成本低廉,环保无污染,对规模化工业生产具有深刻意义。In response to the above problems, the present invention provides a preparation method of cesium-modified phosphotungstic acid @UiO-66/porous carbon-based composite material and its application in cellulose dehydration; the catalyst provided by the present invention has high catalytic performance and is synthesized The process is simple, the recycling method is simple, the reusability is excellent, the raw material cost is low, environmentally friendly and pollution-free, and has profound significance for large-scale industrial production.
本发明的技术方案是:本发明公开了一种铯改性的磷钨酸@UiO-66/多孔碳基复合材料的制备方法;其以生物质衍生的多孔碳基材料为载体,铯改性的磷钨酸@UiO-66(CsxH3-xPW12O40@UiO-66)为活性组分,将活性组分均匀分散在多孔碳基材料孔道内,从而制得铯改性的磷钨酸@UiO-66/多孔碳基复合材料(即CsxH3-xPW12O40@UiO-66/生物质多孔碳基复合材料);其具体操作步骤如下:The technical solution of the present invention is: the present invention discloses a preparation method of cesium-modified phosphotungstic acid @UiO-66/porous carbon-based composite material; it uses biomass-derived porous carbon-based material as a carrier, and the cesium-modified Phosphotungstic acid @UiO-66 (Cs x H 3-x PW 12 O 40 @UiO-66) is the active component, and the active component is evenly dispersed in the pores of the porous carbon-based material to prepare cesium-modified Phosphotungstic acid @UiO-66/porous carbon-based composite material (i.e. Cs x H 3-x PW 12 O 40 @UiO-66/biomass porous carbon-based composite material); the specific operation steps are as follows:
步骤(1):将生物质原料与造孔剂充分混合,其中,生物质与造孔剂的质量比为(10~1):1,再加入10~100mL超纯水,加热至沸腾状态,在沸腾状态下进行回流处理2~6h,洗涤,干燥,随后在N2氛围中于500~1000℃下煅烧1~4h,冷却至室温,得到多孔碳基材料;Step (1): Thoroughly mix the biomass raw material and the pore-forming agent, where the mass ratio of the biomass and the pore-forming agent is (10~1):1, then add 10~100mL of ultrapure water, and heat to a boiling state. Perform reflux treatment in a boiling state for 2 to 6 hours, wash, dry, and then calcine at 500 to 1000°C for 1 to 4 hours in an N2 atmosphere, and cool to room temperature to obtain a porous carbon-based material;
步骤(2):将金属盐和对苯二甲酸用含有N,N-二甲基甲酰胺和甲酸的混合溶液溶解,再加入磷钨酸,搅拌均匀,得到H3PW12O40@UiO-66前驱体溶液;Step (2): Dissolve the metal salt and terephthalic acid in a mixed solution containing N,N-dimethylformamide and formic acid, then add phosphotungstic acid and stir evenly to obtain H 3 PW 12 O 40 @UiO- 66 precursor solution;
步骤(3):将多孔碳基材料与H3PW12O40@UiO-66前驱体溶液混合并搅拌均匀,然后在100~220℃下水热12~40h;反应结束后,降温冷却,过滤,乙醇搅拌洗涤3次,过滤干燥得到H3PW12O40@UiO-66/生物质多孔碳基材料;Step (3): Mix the porous carbon-based material and the H 3 PW 12 O 40 @UiO-66 precursor solution and stir evenly, then hydroheat at 100 to 220°C for 12 to 40 hours; after the reaction is completed, cool down and filter. Stir and wash with ethanol 3 times, filter and dry to obtain H 3 PW 12 O 40 @UiO-66/biomass porous carbon-based material;
步骤(4):将H3PW12O40@UiO-66/生物质多孔碳基材料加入到铯盐溶液中,搅拌6~12h,静置6~12h,控制在60~100℃旋转蒸发至干,即得到铯改性的磷钨酸@UiO-66/多孔碳基复合材料(CsxH3-xPW12O40@UiO-66/多孔碳基材料)。Step (4): Add H 3 PW 12 O 40 @UiO-66/biomass porous carbon-based material to the cesium salt solution, stir for 6 to 12 hours, let stand for 6 to 12 hours, and control the rotary evaporation at 60 to 100°C. After drying, the cesium-modified phosphotungstic acid @UiO-66/porous carbon-based composite material (Cs x H 3-x PW 12 O 40 @UiO-66/porous carbon-based material) is obtained.
进一步的,在步骤(1)中,所述的生物质原料是杨木,竹子,大豆秸秆及果壳中任意一种;Further, in step (1), the biomass raw material is any one of poplar, bamboo, soybean straw and fruit shell;
所述的造孔剂为乙酰丙酮锌、葡萄糖酸锌、乙酸锌及草酸锌中的任意一种;The pore-forming agent is any one of zinc acetylacetonate, zinc gluconate, zinc acetate and zinc oxalate;
所述生物质原料与造孔剂的质量比为:10~1:1;The mass ratio of the biomass raw material to the pore-forming agent is: 10 to 1:1;
所述加入的超纯水的体积为:10~100mL;The volume of ultrapure water added is: 10 to 100 mL;
所述沸腾状态为:100~120℃;The boiling state is: 100~120℃;
所述室温:15~30℃。The room temperature is: 15~30℃.
进一步的,在步骤(2)中,所述金属盐为氯化锆,氯化铪,氯化铈的任一种;Further, in step (2), the metal salt is any one of zirconium chloride, hafnium chloride, and cerium chloride;
所述磷钨酸、对苯二甲酸与金属盐的质量比为(100~1):1:(10~1);所述混合溶液中N,N-二甲基甲酰胺与甲酸的体积比为(20~1):1。The mass ratio of the phosphotungstic acid, terephthalic acid and metal salt is (100~1):1:(10~1); the volume ratio of N,N-dimethylformamide and formic acid in the mixed solution It is (20~1):1.
进一步的,在步骤(3)中,所述多孔碳基材料与H3PW12O40@UiO-66前驱体中的质量比为1:(50~1)。Further, in step (3), the mass ratio of the porous carbon-based material to the H 3 PW 12 O 40 @UiO-66 precursor is 1: (50~1).
进一步的,在步骤(4)中,所述铯盐为碳酸铯,硝酸铯、乙酸铯中的任意一种;Further, in step (4), the cesium salt is any one of cesium carbonate, cesium nitrate, and cesium acetate;
所述铯盐与H3PW12O40@UiO-66/生物质多孔碳基材料的质量比为1:(50~1)。The mass ratio of the cesium salt to H 3 PW 12 O 40 @UiO-66/biomass porous carbon-based material is 1: (50~1).
进一步的,所述该制备方法制备的CsxH3-xPW12O40@UiO-66/多孔碳基复合材料在纤维素脱水反应中的应用;其具体的条件是:在高压反应釜中催化纤维素脱水转化制备5-羟甲基糠醛的应用方法,将纤维素与双相溶剂H2O/THF以质量比为1:(40~80)配置为溶液装入到高压反应釜中,保持催化剂与纤维素原料的质量比为1:(2~20),H2O与THF的体积比为1:(6~3),通入N2作为保护气并调节系统初始压力为0.5~1.5MPa,反应温度为160~240℃,升温速率为5~15℃/min,反应时间为1~5h,搅拌速度为500~1200r/min。Further, the application of the Cs x H 3-x PW 12 O 40 @UiO-66/porous carbon-based composite material prepared by this preparation method in cellulose dehydration reaction; the specific conditions are: in a high-pressure reactor The application method of catalyzing the dehydration and conversion of cellulose to prepare 5-hydroxymethylfurfural is to prepare a solution of cellulose and biphasic solvent H 2 O/THF at a mass ratio of 1: (40-80) and put it into a high-pressure reaction kettle. Keep the mass ratio of catalyst to cellulose raw material as 1: (2~20), the volume ratio of H 2 O and THF as 1: (6~3), introduce N 2 as protective gas and adjust the initial pressure of the system to 0.5~ 1.5MPa, the reaction temperature is 160~240℃, the heating rate is 5~15℃/min, the reaction time is 1~5h, and the stirring speed is 500~1200r/min.
本发明的有益效果是:本发明的特点是:1、本发明研究了纤维素脱水转化获取5-HMF,能有效缓解化石能源过度消耗引起的环境污染问题,同时降低对不可再生能源的依赖,对可持续发展战略具有关键作用;2、本方法采用生物质为前驱体制备的多孔碳基材料作为载体,原料为天然可再生,来源广泛,成本低廉,环保无污染;3、本方法优化了传统的生产工艺,合成工艺简单,实现了纤维素的高效率转化,回收方式简单高效,重复利用性能优异,有利于规模化工业生产。The beneficial effects of the present invention are: The characteristics of the present invention are: 1. The present invention studies the dehydration and transformation of cellulose to obtain 5-HMF, which can effectively alleviate the environmental pollution problems caused by excessive consumption of fossil energy and reduce the dependence on non-renewable energy. It plays a key role in sustainable development strategy; 2. This method uses porous carbon-based materials prepared from biomass as a precursor as a carrier. The raw materials are natural and renewable, with wide sources, low cost, environmental protection and pollution-free; 3. This method optimizes The traditional production process and simple synthesis process achieve high-efficiency conversion of cellulose, the recycling method is simple and efficient, and the reuse performance is excellent, which is conducive to large-scale industrial production.
附图说明Description of drawings
图1是本发明的操作流程图;Figure 1 is an operation flow chart of the present invention;
图2是本发明实施例4制得的CsxH3-xPW12O40@UiO-66(Hf)/多孔杨木碳基复合材料材料的SEM形貌图。Figure 2 is an SEM morphology image of the Cs x H 3-x PW 12 O 40 @UiO-66(Hf)/porous poplar carbon-based composite material prepared in Example 4 of the present invention.
具体实施方式Detailed ways
为了更清楚地说明本发明的技术方案,下面结合附图对本发明的技术方案做进一步的详细说明:In order to explain the technical solution of the present invention more clearly, the technical solution of the present invention will be further described in detail below with reference to the accompanying drawings:
如图所述,本发明所述的CsxH3-xPW12O40@UiO-66/多孔碳基复合材料,以生物质衍生的多孔碳基材料为载体,铯改性的磷钨酸@UiO-66(CsxH3-xPW12O40@UiO-66)为活性组分,其中活性组分均匀分散在多孔碳基材料孔道内;其具体操作步骤如下:As shown in the figure , the Cs @UiO-66 (Cs x H 3-x PW 12 O 40 @UiO-66) is an active component, in which the active component is evenly dispersed in the pores of the porous carbon-based material; the specific operation steps are as follows:
步骤1:将生物质原料与造孔剂充分混合,其中,生物质与造孔剂的质量比为(10~1):1,再加入10~00mL超纯水,在沸腾状态下进行回流处理2~6h,洗涤,干燥,随后在N2氛围中于500~1000℃下煅烧1~4h,冷却至室温,得到多孔碳基材料;Step 1: Thoroughly mix the biomass raw material and the pore-forming agent. The mass ratio of the biomass and the pore-forming agent is (10~1):1. Then add 10~00mL ultrapure water and perform reflux treatment in the boiling state. 2 to 6 hours, washing, drying, and then calcining at 500 to 1000°C for 1 to 4 hours in a N2 atmosphere, and cooling to room temperature to obtain a porous carbon-based material;
步骤2:将金属盐和对苯二甲酸用N,N-二甲基甲酰胺和甲酸的混合溶液溶解,再加入磷钨酸,搅拌均匀,得到H3PW12O40@UiO-66前驱体溶液;Step 2: Dissolve the metal salt and terephthalic acid with a mixed solution of N,N-dimethylformamide and formic acid, then add phosphotungstic acid, stir evenly, and obtain the H 3 PW 12 O 40 @UiO-66 precursor. solution;
步骤3:将生物质多孔碳基材料与H3PW12O40@UiO-66前驱体溶液混合并搅拌均匀,然后在100~220℃下水热12~40h;反应结束后,降温冷却,过滤,乙醇搅拌洗涤3次,过滤干燥得到H3PW12O40@UiO-66/生物质多孔碳基材料;Step 3: Mix the biomass porous carbon-based material and H 3 PW 12 O 40 @UiO-66 precursor solution and stir evenly, then hydroheat at 100-220°C for 12-40 hours; after the reaction is completed, cool down and filter. Stir and wash with ethanol 3 times, filter and dry to obtain H 3 PW 12 O 40 @UiO-66/biomass porous carbon-based material;
步骤4:将H3PW12O40@UiO-66/生物质多孔碳基材料加入到铯盐溶液中,搅拌6~12h,静置6~12h,控制在60~100℃旋转蒸发至干,即得到铯改性的CsxH3-xPW12O40@UiO-66/多孔碳基复合材料;Step 4: Add H 3 PW 12 O 40 @UiO-66/biomass porous carbon-based material to the cesium salt solution, stir for 6 to 12 hours, let stand for 6 to 12 hours, and control the rotary evaporation to dryness at 60 to 100°C. That is, the cesium-modified Cs x H 3-x PW 12 O 40 @UiO-66/porous carbon-based composite material is obtained;
下面通过实施例对本发明技术方案作进一步详细说明。The technical solution of the present invention will be further described in detail below through examples.
实施例1Example 1
将1.5g杨木与1g葡萄糖酸锌充分混合,再加入50mL超纯水,在沸腾状态下进行回流处理4h,洗涤,干燥,随后在N2氛围中于800℃下煅烧2h,冷却至室温,得到多孔杨木碳基材料。Thoroughly mix 1.5g poplar wood and 1g zinc gluconate, then add 50mL ultrapure water, perform reflux treatment in a boiling state for 4h, wash, dry, and then calcine at 800°C for 2h in a N2 atmosphere, and cool to room temperature. Porous poplar carbon-based materials were obtained.
实施例2Example 2
将0.48g氯化铪和0.27g对苯二甲酸用54mL的N,N-二甲基甲酰胺和6mL的甲酸混合溶液溶解,再加入0.3g磷钨酸,得到H3PW12O40@UiO-66前驱体溶液。Dissolve 0.48g hafnium chloride and 0.27g terephthalic acid with a mixed solution of 54mL N,N-dimethylformamide and 6mL formic acid, then add 0.3g phosphotungstic acid to obtain H 3 PW 12 O 40 @UiO -66 precursor solution.
实施例3Example 3
将1.0g生物质多孔碳基材料与H3PW12O40@UiO-66前驱体溶液混合并搅拌均匀,然后在100~220℃下水热12~40h;反应结束后,降温冷却,过滤,乙醇搅拌洗涤3次,过滤干燥得到H3PW12O40@UiO-66/生物质多孔碳基材料。Mix 1.0g of biomass porous carbon-based material and H 3 PW 12 O 40 @UiO-66 precursor solution and stir evenly, then hydrotherm at 100 to 220°C for 12 to 40 hours; after the reaction is completed, cool down, filter, and add ethanol Stir and wash 3 times, filter and dry to obtain H 3 PW 12 O 40 @UiO-66/biomass porous carbon-based material.
实施例4Example 4
将1g的H3PW12O40@UiO-66/生物质多孔碳基材料加入50mL的5wt%硝酸铯溶液中,搅拌12h,静置12h,控制在60℃旋转蒸发至干,即得到CsxH3-xPW12O40@UiO-66/生物质多孔碳基材料.Add 1g of H 3 PW 12 O 40 @UiO-66/biomass porous carbon-based material into 50mL of 5wt% cesium nitrate solution, stir for 12h, let stand for 12h, control the rotary evaporation to dryness at 60°C, and obtain Cs x H 3-x PW 12 O 40 @UiO-66/biomass porous carbon-based materials.
实施例5Example 5
取1.0g制备好的CsxH3-xPW12O40@UiO-66/生物质多孔碳基材料催化剂、2.5g纤维素、20mL蒸馏水、30mL四氢呋喃置于到高压反应釜中。通入1MPa的氮气,放空,重复三次除去反应釜内的空气。调节加热温度为180℃,升温速率为10℃/min,反应时间为4h,搅拌速度为800r/min。Take 1.0g of the prepared Cs x H 3-x PW 12 O 40 @UiO-66/biomass porous carbon-based material catalyst, 2.5g of cellulose, 20mL of distilled water, and 30mL of tetrahydrofuran and place them into a high-pressure reaction kettle. Pour in 1MPa of nitrogen, vent, and repeat three times to remove the air in the reaction kettle. Adjust the heating temperature to 180°C, the heating rate to 10°C/min, the reaction time to 4h, and the stirring speed to 800r/min.
实施例6Example 6
几种CsxH3-xPW12O40@UiO-66/生物质多孔碳基材料的催化性能见表1,反应条件同实施例5。The catalytic properties of several Cs x H 3-x PW 12 O 40 @UiO-66/biomass porous carbon-based materials are shown in Table 1. The reaction conditions are the same as in Example 5.
表1几种CsxH3-xPW12O40@UiO-66/生物质多孔碳基材料催化剂的催化性能比较;Table 1 Comparison of catalytic performance of several Cs x H 3-x PW 12 O 40 @UiO-66/biomass porous carbon-based material catalysts;
最后,应当理解的是,本发明中所述实施例仅用以说明本发明实施例的原则;其他的变形也可能属于本发明的范围;因此,作为示例而非限制,本发明实施例的替代配置可视为与本发明的教导一致;相应地,本发明的实施例不限于本发明明确介绍和描述的实施例。Finally, it should be understood that the embodiments described in the present invention are only used to illustrate the principles of the embodiments of the present invention; other modifications may also fall within the scope of the present invention; therefore, alternatives to the embodiments of the present invention are provided as examples rather than limitations. Configurations may be considered consistent with the teachings of the invention; accordingly, embodiments of the invention are not limited to those expressly introduced and described herein.
Claims (6)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202210579623.3A CN114904587B (en) | 2022-05-26 | 2022-05-26 | Preparation method of cesium modified phosphotungstic acid@UiO-66/porous carbon-based composite material |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202210579623.3A CN114904587B (en) | 2022-05-26 | 2022-05-26 | Preparation method of cesium modified phosphotungstic acid@UiO-66/porous carbon-based composite material |
Publications (2)
Publication Number | Publication Date |
---|---|
CN114904587A CN114904587A (en) | 2022-08-16 |
CN114904587B true CN114904587B (en) | 2024-02-23 |
Family
ID=82768495
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN202210579623.3A Active CN114904587B (en) | 2022-05-26 | 2022-05-26 | Preparation method of cesium modified phosphotungstic acid@UiO-66/porous carbon-based composite material |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN114904587B (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN116371473B (en) * | 2023-04-19 | 2024-07-09 | 大连理工大学宁波研究院 | Composite catalyst for olefin epoxidation reaction, preparation method and application thereof |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108772100A (en) * | 2018-05-22 | 2018-11-09 | 广东工业大学 | A kind of heteropolyacid salt solid catalyst and its preparation method and application |
CN110256683A (en) * | 2019-04-19 | 2019-09-20 | 武汉理工大学 | A kind of preparation method and applications of hierarchical porous structure metal-organic framework materials |
CN111359663A (en) * | 2020-02-19 | 2020-07-03 | 浙江工业大学 | Application of a catalyst based on organometallic framework UiO-66 in cellulose hydrolysis |
CN112354563A (en) * | 2020-11-27 | 2021-02-12 | 广东省科学院生物工程研究所 | Carbon catalyst loaded with phosphotungstic acid, and preparation method and application thereof |
-
2022
- 2022-05-26 CN CN202210579623.3A patent/CN114904587B/en active Active
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108772100A (en) * | 2018-05-22 | 2018-11-09 | 广东工业大学 | A kind of heteropolyacid salt solid catalyst and its preparation method and application |
CN110256683A (en) * | 2019-04-19 | 2019-09-20 | 武汉理工大学 | A kind of preparation method and applications of hierarchical porous structure metal-organic framework materials |
CN111359663A (en) * | 2020-02-19 | 2020-07-03 | 浙江工业大学 | Application of a catalyst based on organometallic framework UiO-66 in cellulose hydrolysis |
CN112354563A (en) * | 2020-11-27 | 2021-02-12 | 广东省科学院生物工程研究所 | Carbon catalyst loaded with phosphotungstic acid, and preparation method and application thereof |
Non-Patent Citations (3)
Title |
---|
12-Tungstophosphoric acid-encapsulated metal-organic framework UiO-66: A promising catalyst for the esterification of acetic acid with nbutanol;Tianlin Ma等;《Journal of the Taiwan Institute of Chemical Engineers》;104277 * |
Phosphotungstic acid encapsulated in metal-organic framework UiO-66: An effective catalyst for the selective oxidation of cyclopentene to glutaraldehyde;Xin-Li Yang等;《Microporous and Mesoporous Materials》;73-81 * |
Synthesis of polyoxometalate encapsulated in UiO-66(Zr) with hierarchical porosity and double active sites for oxidation desulfurization of fuel oil at room temperature;Gan Ye等;《J. Mater. Chem. A》;19396-19404 * |
Also Published As
Publication number | Publication date |
---|---|
CN114904587A (en) | 2022-08-16 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN111377890B (en) | Method for producing 2,5-furandicarboxylic acid from 5-hydroxymethylfurfural | |
CN106582655B (en) | Preparation method of high-dispersion easy-reduction supported nickel-aluminum catalyst | |
CN112121863B (en) | A kind of catalyst for catalytic transfer hydrogenation and its preparation method and application | |
CN108745333B (en) | A kind of porous carbon aerogel catalyst and its preparation method and application | |
CN108671960A (en) | A kind of high hydrothermal stability MOFs catalyst, the method for preparing and preparing chemicals for cellulose conversion | |
CN110152663A (en) | Catalyst for producing furfuryl alcohol by gas-phase hydrogenation of furfural and its preparation and application | |
CN110690468B (en) | Preparation and application of single-atom platinum catalysts based on platinum-coordinated cyclodextrin inclusion complexes | |
CN114570429A (en) | Monoatomic-supported covalent organic framework material, preparation thereof and application thereof in hydrogen production by photolysis of water | |
CN106807387B (en) | A kind of bifunctional catalyst and preparation method thereof for absorption enhancement hydrogen production by bio-oil steam reforming | |
CN104667913A (en) | Macroporous aluminum oxide assembled nano metal catalyst as well as preparation and application to methanol liquid-phase catalytic reaction | |
CN114904587B (en) | Preparation method of cesium modified phosphotungstic acid@UiO-66/porous carbon-based composite material | |
CN112023924A (en) | Preparation method and application of copper-based catalyst loaded with rubber seed shell porous activated carbon | |
CN113289692B (en) | A kind of magnetic biomass solid catalyst and its preparation and application | |
CN114570389A (en) | Sulfonic acid-based carbon catalyst and preparation method and application thereof | |
CN110882716B (en) | Preparation method of solid acid catalyst for one-pot multi-step catalytic conversion of biomass-derived furfural into γ-valerolactone | |
CN107286006A (en) | A kind of method that catalyzed alcoholysis lignin prepares Acetovanillone and acetosyringone | |
CN106902827B (en) | Preparation method and application of catalyst with nickel loaded on attapulgite as carrier | |
CN107497490B (en) | Preparation method of metal organic gel loaded CdS catalyst and application of catalyst in hydrogen production through photolysis of water | |
CN106378161B (en) | Dimethyl ether is for the carbon containing porous material catalyst and preparation method of polymethoxy dimethyl ether and application | |
CN112371188B (en) | A kind of preparation method of high-efficiency methanation nano-catalyst | |
CN116020455A (en) | Catalyst for promoting hydrogenation of carbon dioxide to prepare methanol and application thereof | |
CN104148105B (en) | By porous catalyst of direct synthesis of dimethyl ether from synthesis gas and its preparation method and application | |
CN109622010B (en) | A method for dehydrogenation of formaldehyde catalyzed by Pd@CNx mosaic catalyst | |
CN114315553A (en) | A kind of method that solid acid catalyzes glucose to prepare levulinic acid in hydrophilic DES | |
CN106512981A (en) | Vanadium-based catalyst for preparation of phenol through direct oxidation of benzene and preparation method thereof |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
GR01 | Patent grant | ||
GR01 | Patent grant |