CN109985654A - A kind of alkali metal ion modified carbon nitride catalyst and its preparation method and application - Google Patents
A kind of alkali metal ion modified carbon nitride catalyst and its preparation method and application Download PDFInfo
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- JMANVNJQNLATNU-UHFFFAOYSA-N oxalonitrile Chemical class N#CC#N JMANVNJQNLATNU-UHFFFAOYSA-N 0.000 title claims abstract description 50
- 239000003054 catalyst Substances 0.000 title claims abstract description 32
- 229910001413 alkali metal ion Inorganic materials 0.000 title claims abstract description 27
- 238000002360 preparation method Methods 0.000 title claims abstract description 9
- 238000006460 hydrolysis reaction Methods 0.000 claims abstract description 18
- 230000007062 hydrolysis Effects 0.000 claims abstract description 17
- 230000009881 electrostatic interaction Effects 0.000 claims abstract description 4
- JJWKPURADFRFRB-UHFFFAOYSA-N carbonyl sulfide Chemical compound O=C=S JJWKPURADFRFRB-UHFFFAOYSA-N 0.000 claims description 47
- -1 thiocyanic acid amine Chemical class 0.000 claims description 24
- 238000000034 method Methods 0.000 claims description 17
- 239000000843 powder Substances 0.000 claims description 14
- WCUXLLCKKVVCTQ-UHFFFAOYSA-M Potassium chloride Chemical compound [Cl-].[K+] WCUXLLCKKVVCTQ-UHFFFAOYSA-M 0.000 claims description 10
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 claims description 8
- 239000012298 atmosphere Substances 0.000 claims description 8
- 230000004048 modification Effects 0.000 claims description 8
- 238000012986 modification Methods 0.000 claims description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 8
- 239000007787 solid Substances 0.000 claims description 7
- 229920000877 Melamine resin Polymers 0.000 claims description 6
- JDSHMPZPIAZGSV-UHFFFAOYSA-N melamine Chemical compound NC1=NC(N)=NC(N)=N1 JDSHMPZPIAZGSV-UHFFFAOYSA-N 0.000 claims description 6
- 239000001103 potassium chloride Substances 0.000 claims description 5
- 235000011164 potassium chloride Nutrition 0.000 claims description 5
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 claims description 4
- 239000002585 base Substances 0.000 claims description 4
- 238000001354 calcination Methods 0.000 claims description 4
- IOLCXVTUBQKXJR-UHFFFAOYSA-M potassium bromide Chemical compound [K+].[Br-] IOLCXVTUBQKXJR-UHFFFAOYSA-M 0.000 claims description 4
- JHJLBTNAGRQEKS-UHFFFAOYSA-M sodium bromide Chemical compound [Na+].[Br-] JHJLBTNAGRQEKS-UHFFFAOYSA-M 0.000 claims description 4
- 239000011780 sodium chloride Substances 0.000 claims description 4
- UMGDCJDMYOKAJW-UHFFFAOYSA-N thiourea Chemical compound NC(N)=S UMGDCJDMYOKAJW-UHFFFAOYSA-N 0.000 claims description 4
- 239000000203 mixture Substances 0.000 claims description 3
- LYQFWZFBNBDLEO-UHFFFAOYSA-M caesium bromide Chemical compound [Br-].[Cs+] LYQFWZFBNBDLEO-UHFFFAOYSA-M 0.000 claims description 2
- AIYUHDOJVYHVIT-UHFFFAOYSA-M caesium chloride Chemical compound [Cl-].[Cs+] AIYUHDOJVYHVIT-UHFFFAOYSA-M 0.000 claims description 2
- 239000004202 carbamide Substances 0.000 claims description 2
- STIAPHVBRDNOAJ-UHFFFAOYSA-N carbamimidoylazanium;carbonate Chemical compound NC(N)=N.NC(N)=N.OC(O)=O STIAPHVBRDNOAJ-UHFFFAOYSA-N 0.000 claims description 2
- 239000008367 deionised water Substances 0.000 claims description 2
- 229910021641 deionized water Inorganic materials 0.000 claims description 2
- QGBSISYHAICWAH-UHFFFAOYSA-N dicyandiamide Chemical compound NC(N)=NC#N QGBSISYHAICWAH-UHFFFAOYSA-N 0.000 claims description 2
- ZMZDMBWJUHKJPS-UHFFFAOYSA-N hydrogen thiocyanate Natural products SC#N ZMZDMBWJUHKJPS-UHFFFAOYSA-N 0.000 claims description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims 4
- 239000003513 alkali Substances 0.000 claims 4
- 150000004820 halides Chemical class 0.000 claims 3
- 229910052757 nitrogen Inorganic materials 0.000 claims 2
- 150000002894 organic compounds Chemical class 0.000 claims 2
- 150000001412 amines Chemical class 0.000 claims 1
- XKMRRTOUMJRJIA-UHFFFAOYSA-N ammonia nh3 Chemical compound N.N XKMRRTOUMJRJIA-UHFFFAOYSA-N 0.000 claims 1
- 230000005595 deprotonation Effects 0.000 claims 1
- 238000010537 deprotonation reaction Methods 0.000 claims 1
- 229910021645 metal ion Inorganic materials 0.000 claims 1
- 230000003197 catalytic effect Effects 0.000 abstract description 3
- CREXVNNSNOKDHW-UHFFFAOYSA-N azaniumylideneazanide Chemical class N[N] CREXVNNSNOKDHW-UHFFFAOYSA-N 0.000 abstract description 2
- 125000001741 organic sulfur group Chemical group 0.000 abstract description 2
- 229910052700 potassium Inorganic materials 0.000 description 17
- 239000011591 potassium Substances 0.000 description 17
- 229910052783 alkali metal Inorganic materials 0.000 description 8
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 7
- 238000001816 cooling Methods 0.000 description 7
- 230000000694 effects Effects 0.000 description 6
- 238000005470 impregnation Methods 0.000 description 6
- 238000006555 catalytic reaction Methods 0.000 description 5
- 229910001514 alkali metal chloride Inorganic materials 0.000 description 4
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 4
- 230000015572 biosynthetic process Effects 0.000 description 4
- 239000012299 nitrogen atmosphere Substances 0.000 description 4
- 229910001414 potassium ion Inorganic materials 0.000 description 4
- 239000011734 sodium Substances 0.000 description 4
- 238000003786 synthesis reaction Methods 0.000 description 4
- 229910001508 alkali metal halide Inorganic materials 0.000 description 3
- 150000008045 alkali metal halides Chemical class 0.000 description 3
- 150000008044 alkali metal hydroxides Chemical class 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 238000001570 ionothermal synthesis Methods 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 238000013507 mapping Methods 0.000 description 3
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 3
- 229910001415 sodium ion Inorganic materials 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 229910052723 transition metal Inorganic materials 0.000 description 3
- 150000003624 transition metals Chemical class 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 238000005033 Fourier transform infrared spectroscopy Methods 0.000 description 2
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 2
- 230000005540 biological transmission Effects 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 229910002804 graphite Inorganic materials 0.000 description 2
- 239000010439 graphite Substances 0.000 description 2
- 230000003993 interaction Effects 0.000 description 2
- 229910044991 metal oxide Inorganic materials 0.000 description 2
- 150000004706 metal oxides Chemical class 0.000 description 2
- 238000000634 powder X-ray diffraction Methods 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- BCHZICNRHXRCHY-UHFFFAOYSA-N 2h-oxazine Chemical group N1OC=CC=C1 BCHZICNRHXRCHY-UHFFFAOYSA-N 0.000 description 1
- XZMCDFZZKTWFGF-UHFFFAOYSA-N Cyanamide Chemical compound NC#N XZMCDFZZKTWFGF-UHFFFAOYSA-N 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- CKUAXEQHGKSLHN-UHFFFAOYSA-N [C].[N] Chemical compound [C].[N] CKUAXEQHGKSLHN-UHFFFAOYSA-N 0.000 description 1
- 230000009102 absorption Effects 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 150000001340 alkali metals Chemical class 0.000 description 1
- 125000003277 amino group Chemical group 0.000 description 1
- 125000003118 aryl group Chemical group 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000000969 carrier Substances 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 230000009849 deactivation Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 125000000623 heterocyclic group Chemical group 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- LELOWRISYMNNSU-UHFFFAOYSA-N hydrogen cyanide Chemical compound N#C LELOWRISYMNNSU-UHFFFAOYSA-N 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 238000011068 loading method Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000003345 natural gas Substances 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 231100000252 nontoxic Toxicity 0.000 description 1
- 230000003000 nontoxic effect Effects 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 230000001699 photocatalysis Effects 0.000 description 1
- 238000006303 photolysis reaction Methods 0.000 description 1
- 230000015843 photosynthesis, light reaction Effects 0.000 description 1
- 231100000572 poisoning Toxicity 0.000 description 1
- 230000000607 poisoning effect Effects 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000006722 reduction reaction Methods 0.000 description 1
- 230000029058 respiratory gaseous exchange Effects 0.000 description 1
- 239000004065 semiconductor Substances 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 238000001228 spectrum Methods 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 238000001308 synthesis method Methods 0.000 description 1
Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/86—Catalytic processes
- B01D53/8603—Removing sulfur compounds
- B01D53/8606—Removing sulfur compounds only one sulfur compound other than sulfur oxides or hydrogen sulfide
-
- 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
- B01J27/00—Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
- B01J27/24—Nitrogen compounds
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/30—Sulfur compounds
- B01D2257/308—Carbonoxysulfide COS
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- Chemical Kinetics & Catalysis (AREA)
- Health & Medical Sciences (AREA)
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Abstract
本发明属于催化剂技术领域,具体涉及一种碱金属离子修饰的氮化碳催化剂、其制备方法及应用。所述催化剂,以氮化碳为主体,所述修饰的碱金属离子包括Na+、K+和Cs+其中的一种或几种的组合,其中碱金属离子的含量0.1~10wt%;所述催化剂中的碱金属离子通过静电相互作用吸附在氮化碳去质子化的氨基氮上。本发明的催化剂可作为有机硫水解催化剂,表现出了良好的催化活性和稳定性。
The invention belongs to the technical field of catalysts, and in particular relates to an alkali metal ion modified carbon nitride catalyst, a preparation method and application thereof. The catalyst is mainly composed of carbon nitride, the modified alkali metal ions include one or a combination of Na + , K + and Cs + , wherein the content of the alkali metal ions is 0.1-10 wt %; the The alkali metal ions in the catalyst are adsorbed on the deprotonated amino nitrogen of carbon nitride through electrostatic interaction. The catalyst of the present invention can be used as an organic sulfur hydrolysis catalyst, and exhibits good catalytic activity and stability.
Description
技术领域technical field
本发明属于催化剂技术领域,具体涉及一种碱金属离子修饰的氮化碳催化剂、其制备方法及应用。The invention belongs to the technical field of catalysts, and in particular relates to an alkali metal ion modified carbon nitride catalyst, a preparation method and application thereof.
背景技术Background technique
羰基硫(COS)作为一种有机硫的主要存在形式,广泛存在于煤、天然气和石油等化石原料中。工业生产中微量的COS很容易引起生产工序中催化剂中毒失活、生产设备与仪器腐蚀并影响化工产品质量;此外,不经处理的COS排放到大气中,会与氧作用形成SO2,促进光化学反应,带来严重的污染环境,对人类健康产生威胁。羰基硫的物理化学性质稳定,呈弱酸性,与H2S相比,既不易离解也不易液化,一般用于脱除H2S的方法不能完全有效直接脱除COS。目前,COS的主要脱除技术有水解法、还原法、吸收法、吸附法、光解法及氧化法等,其中利用水解法来脱除COS被证明是最有效的方法之一,其基本原理是:COS在催化剂作用下和水反应转化为H2S,然后再通过其它方法脱除H2S,整个过程操作简单,能量耗费较低。水解法的关键技术是开发出高效经济的催化剂。Carbonyl sulfide (COS), as the main form of organic sulfur, widely exists in fossil raw materials such as coal, natural gas and petroleum. A trace amount of COS in industrial production can easily cause catalyst poisoning and deactivation in the production process, corrosion of production equipment and instruments, and affect the quality of chemical products; in addition, untreated COS is discharged into the atmosphere, which will react with oxygen to form SO 2 , which promotes photochemistry. The reaction will bring serious pollution to the environment and pose a threat to human health. Carbonyl sulfide has stable physical and chemical properties and is weakly acidic. Compared with H 2 S, it is neither easy to dissociate nor liquefy. The methods generally used to remove H 2 S cannot completely and effectively remove COS directly. At present, the main removal technologies of COS include hydrolysis, reduction, absorption, adsorption, photolysis and oxidation. Among them, hydrolysis to remove COS has been proved to be one of the most effective methods. The basic principle is that : COS reacts with water to convert into H 2 S under the action of a catalyst, and then removes H 2 S by other methods. The whole process is simple to operate and has low energy consumption. The key technology of hydrolysis is to develop efficient and economical catalysts.
目前的COS水解催化剂大多选用金属氧化物或活性炭作为载体,并进一步在该金属氧化物或活性炭上负载活性组分后制备得到。这类负载型的COS水解催化剂大部分含有过渡金属,价格昂贵,并且存在制备工艺复杂、活性组分容易从载体脱落、活性稳定性差等缺点。因此,通过对COS水解催化剂的创新,发明一种不含过渡金属且活性组分与载体具有强的相互作用的COS水解催化剂具有新颖性。Most of the current COS hydrolysis catalysts use metal oxides or activated carbons as carriers, and are prepared by loading active components on the metal oxides or activated carbons. Most of these supported COS hydrolysis catalysts contain transition metals, which are expensive, and have disadvantages such as complicated preparation process, easy detachment of active components from the carrier, and poor activity stability. Therefore, through the innovation of COS hydrolysis catalyst, it is novel to invent a COS hydrolysis catalyst that does not contain transition metals and has a strong interaction between active components and supports.
近年来,由碳和氮丰富元素组成的具有类石墨结构的氮化碳收到广泛关注。氮化碳聚合物具有良好的耐热耐化学腐蚀,无毒且价格低廉,良好的生物相容性和半导体性质,目前在能源和催化领域具有非常好的应用前景。氮化碳表面具有丰富的未聚合完全的氨基基团,可作为一种理想的碱催化剂和负载型催化剂载体。COS水解反应为碱催化反应,而采用离子热法合成的碱金属离子修饰的氮化碳具有强碱性并且碱金属离子可通过静电相互作用吸附在氮化碳载体上不易脱落、分散性好。因此,碱金属离子修饰的氮化碳有望成为一类COS水解的高效催化剂。In recent years, carbon nitrides with graphitic-like structures composed of carbon- and nitrogen-rich elements have received extensive attention. Carbon nitride polymers have good heat and chemical resistance, non-toxic and inexpensive, good biocompatibility and semiconductor properties, and currently have very good application prospects in the fields of energy and catalysis. The carbon nitride surface has abundant unpolymerized amino groups, which can be used as an ideal base catalyst and supported catalyst carrier. The COS hydrolysis reaction is an alkali-catalyzed reaction, and the alkali metal ion-modified carbon nitride synthesized by the ionothermal method has strong basicity, and the alkali metal ions can be adsorbed on the carbon nitride support through electrostatic interaction, which is not easy to fall off and has good dispersibility. Therefore, alkali metal ion-modified carbon nitride is expected to be an efficient catalyst for a class of COS hydrolysis.
江静等在《催化学报》中公开了一种碱金属掺杂的石墨相氮化碳在可见光光催化制氢中的比较研究,其采用碱金属氢氧化物对氮化碳进行掺杂,但由于碱金属氢氧化物具有强碱性,使得石墨相氮化碳和碱金属氢氧化物在高温处理过程中氮化碳主体结构易遭到破坏,导致石墨相氮化碳的结晶度下降。因此,л共轭体系下降,碱性不高。而本发明采用离子热法合成碱金属离子修饰的氮化碳中,采用中性的碱金属卤化物作为离子溶剂与氮化碳在高温中反应,极大地提高了氮化碳的结晶度,扩展了л共轭体系。因此,所合成的碱金属离子修饰的氮化碳具有强碱性。In the Journal of Catalysis, Jiang Jing et al. disclosed a comparative study of an alkali metal doped graphitic carbon nitride in visible light photocatalytic hydrogen production, which used alkali metal hydroxide to dope carbon nitride, but Due to the strong alkalinity of the alkali metal hydroxide, the main structure of the carbon nitride in the graphite phase and the alkali metal hydroxide is easily damaged during the high temperature treatment, resulting in a decrease in the crystallinity of the graphite phase carbon nitride. Therefore, the π-conjugated system decreases and the basicity is not high. In the present invention, in the synthesis of alkali metal ion-modified carbon nitride by ionothermal method, neutral alkali metal halide is used as ionic solvent to react with carbon nitride at high temperature, which greatly improves the crystallinity of carbon nitride and expands the π-conjugated system. Therefore, the synthesized alkali metal ion-modified carbon nitride has strong basicity.
发明内容SUMMARY OF THE INVENTION
为了解决现有技术中存在的上述问题和缺陷的至少一个方面,本发明提供了一种碱金属离子修饰的氮化碳羰基硫水解催化剂及其制备方法。In order to solve at least one aspect of the above problems and defects existing in the prior art, the present invention provides an alkali metal ion modified carbon nitride carbonyl sulfide hydrolysis catalyst and a preparation method thereof.
为实现上述目的,本发明采用如下技术方案:To achieve the above object, the present invention adopts the following technical solutions:
本发明第一方面公开了一种碱金属离子修饰的氮化碳催化剂,所述碱金属离子包括Na+、K+和Cs+中的一种或几种,其中碱金属离子的含量0 .1~10wt%。所述催化剂中的碱金属离子通过静电相互作用吸附在氮化碳去质子化的氨基氮上。The first aspect of the present invention discloses a carbon nitride catalyst modified by alkali metal ions, the alkali metal ions include one or more of Na + , K + and Cs + , wherein the content of alkali metal ions is 0.1 ~10 wt%. The alkali metal ions in the catalyst are adsorbed on the deprotonated amino nitrogen of carbon nitride by electrostatic interaction.
本发明第二方面公开了所述的碱金属离子修饰的氮化碳催化剂制备方法,包括以下步骤:The second aspect of the present invention discloses the preparation method of the alkali metal ion modified carbon nitride catalyst, which comprises the following steps:
(1)将含氮有机化合物在空气或氮气气氛下、450-650℃煅烧2-4h,得到氮化碳;(1) calcining nitrogen-containing organic compounds in air or nitrogen atmosphere at 450-650 ℃ for 2-4 hours to obtain carbon nitride;
(2)将步骤(1)得到的氮化碳与碱金属氯化物研磨混合均匀;(2) grinding and mixing the carbon nitride obtained in step (1) with the alkali metal chloride evenly;
(3)将步骤(2)得到的混合物在惰性气氛550-650℃煅烧2-4h,生成碱金属离子修饰的氮化碳;(3) calcining the mixture obtained in step (2) at 550-650° C. for 2-4 hours in an inert atmosphere to generate alkali metal ion-modified carbon nitride;
(4)将步骤(3)得到的固体粉末与去离子水混合,然后过滤,除去未吸附在氮化碳上的碱金属离子,将所得固体干燥至少6h,即得所述的碱金属离子修饰的氮化碳催化剂。(4) Mix the solid powder obtained in step (3) with deionized water, then filter to remove the alkali metal ions not adsorbed on the carbon nitride, and dry the obtained solid for at least 6 hours to obtain the alkali metal ion modification of carbon nitride catalysts.
上述步骤(1)中所述的含氮有机化合物为氰胺、双氰胺、三聚氰胺、硫氰酸胺、硫脲、碳酸胍和尿素中的一种或几种。The nitrogen-containing organic compound described in the above step (1) is one or more of cyanamide, dicyandiamide, melamine, amine thiocyanate, thiourea, guanidine carbonate and urea.
上述步骤(2)所述碱金属卤化物为氯化钠、氯化钾、氯化铯、溴化钠、溴化钾和溴化铯中的一种或几种。氮化碳与碱金属卤化物的质量比为:1:(0.5~50)。The alkali metal halide in the above step (2) is one or more of sodium chloride, potassium chloride, cesium chloride, sodium bromide, potassium bromide and cesium bromide. The mass ratio of carbon nitride to alkali metal halide is: 1:(0.5~50).
本发明第三方面公开了所述的碱金属离子修饰的氮化碳催化剂用于催化水解COS的用途。The third aspect of the present invention discloses the use of the alkali metal ion-modified carbon nitride catalyst for catalytic hydrolysis of COS.
本发明的显著优点在于:The significant advantages of the present invention are:
(1)本发明合成方法安全环保,制备工艺简单,条件温和可控。(1) The synthesis method of the present invention is safe and environmentally friendly, the preparation process is simple, and the conditions are mild and controllable.
(2)本发明合成的碱金属离子修饰的氮化碳催化剂中不含过渡金属,原料廉价;碱金属离子均匀分散在氮化碳上,且与氮化碳具有强相互作用,不易脱落。(2) The alkali metal ion-modified carbon nitride catalyst synthesized by the present invention does not contain transition metals, and the raw materials are cheap; the alkali metal ions are uniformly dispersed on the carbon nitride, have a strong interaction with the carbon nitride, and are not easy to fall off.
(3)本发明合成的碱金属离子修饰的氮化碳催化剂,可用于催化水解COS反应,在10小时的催化反应(70℃)测试中,COS转化率达到92%,且活性未发生明显变化,稳定性好。(3) The carbon nitride catalyst modified by alkali metal ions synthesized in the present invention can be used to catalyze the hydrolysis of COS. In the 10-hour catalytic reaction (70° C.) test, the COS conversion rate reaches 92%, and the activity does not change significantly , good stability.
附图说明Description of drawings
图1为实施例1所得的离子热法合成钾离子修饰的氮化碳和浸渍法合成钾离子负载的氮化碳的X射线粉末衍射图(XRD);Fig. 1 is the X-ray powder diffraction pattern (XRD) of ionothermal synthesis of potassium ion-modified carbon nitride obtained in Example 1 and the synthesis of potassium ion-supported carbon nitride by impregnation method;
图2为实施例1所得的离子热法合成钾离子修饰的氮化碳和浸渍法合成钾离子负载的氮化碳的红外(FTIR)谱图;Fig. 2 is the infrared (FTIR) spectrum of ionothermal synthesis of potassium ion-modified carbon nitride obtained in Example 1 and the synthesis of potassium ion-supported carbon nitride by impregnation method;
图3为实施例1所合成的钾离子修饰的氮化碳透射电镜图(TEM)和mapping图;3 is a transmission electron microscope (TEM) and mapping diagram of potassium ion-modified carbon nitride synthesized in Example 1;
图4为实施例1所合成的钾离子修饰的氮化碳和浸渍法合成钾离子负载的氮化碳催化(70℃) COS水解的活性图。4 is a graph showing the activity of the potassium ion-modified carbon nitride synthesized in Example 1 and the potassium ion-supported carbon nitride synthesized by the impregnation method for catalyzing (70° C.) COS hydrolysis.
具体实施方式Detailed ways
为了使本发明所述的内容更加便于理解,下面结合具体实施方式对本发明所述的技术方案做进一步的说明,但是本发明不仅限于此。In order to make the content of the present invention easier to understand, the technical solutions of the present invention will be further described below with reference to specific embodiments, but the present invention is not limited thereto.
实施例1Example 1
首先称取10g三聚氰胺放于氧化铝坩埚中,在空气气氛中550℃条件下煅烧4h。自然冷却后取出样品研磨成粉末状,得到氮化碳粉末。称取2g氮化碳粉末与10g碱金属氯化物(氯化钾)研磨均匀,在氮气气氛中600℃下煅烧2h,自然冷却后得到的固体在水中超声分散,除去氮化碳表面上游离的钾离子,抽滤后烘干,得到钾离子修饰的氮化碳。First, 10 g of melamine was weighed and placed in an alumina crucible, and calcined at 550 °C for 4 h in an air atmosphere. After natural cooling, the sample was taken out and ground into powder to obtain carbon nitride powder. Weigh 2g of carbon nitride powder and 10g of alkali metal chloride (potassium chloride) and grind them uniformly, calcined at 600 °C for 2h in a nitrogen atmosphere, and the solid obtained after natural cooling is ultrasonically dispersed in water to remove free carbon nitride on the surface. The potassium ions are filtered and dried to obtain potassium ion-modified carbon nitride.
实施例2Example 2
首先称取10g三聚氰胺放于氧化铝坩埚中,在空气气氛中550℃条件下煅烧2h。自然冷却后取出样品研磨成粉末状,得到氮化碳粉末。称取2g氮化碳粉末与10g碱金属氯化物(氯化钠)研磨均匀,在氮气气氛中600℃下煅烧2h,自然冷却后得到的固体在水中超声分散,除去氮化碳表面上游离的钠离子,抽滤后烘干,得到钠离子修饰的氮化碳。First, 10 g of melamine was weighed, placed in an alumina crucible, and calcined at 550 °C for 2 h in an air atmosphere. After natural cooling, the sample was taken out and ground into powder to obtain carbon nitride powder. Weigh 2g of carbon nitride powder and 10g of alkali metal chloride (sodium chloride) and grind them uniformly, calcined at 600 °C for 2h in a nitrogen atmosphere, and the solid obtained after natural cooling is ultrasonically dispersed in water to remove free carbon nitride on the surface. The sodium ions are filtered and dried to obtain sodium ion-modified carbon nitride.
实施例3Example 3
首先称取10g三聚氰胺放于氧化铝坩埚中,在空气气氛中550℃条件下煅烧4h。自然冷却后取出样品研磨成粉末状,得到氮化碳粉末。称取2g氮化碳粉末与10g碱金属氯化物(5g氯化钠和5g氯化钾)研磨均匀,在氮气气氛中600℃下煅烧2h,自然冷却后得到的固体在水中超声分散,除去氮化碳表面上游离钠和钾离子,抽滤后烘干,得到钠和钾离子修饰的氮化碳。First, 10 g of melamine was weighed and placed in an alumina crucible, and calcined at 550 °C for 4 h in an air atmosphere. After natural cooling, the sample was taken out and ground into powder to obtain carbon nitride powder. Weigh 2g of carbon nitride powder and 10g of alkali metal chloride (5g of sodium chloride and 5g of potassium chloride) and grind them uniformly, calcined at 600 °C for 2h in a nitrogen atmosphere, and the solid obtained after natural cooling is ultrasonically dispersed in water, remove Free sodium and potassium ions on the surface of carbon nitride are filtered and dried to obtain carbon nitride modified by sodium and potassium ions.
对比例1Comparative Example 1
首先称取10g三聚氰胺放于氧化铝坩埚中,在空气气氛中550℃条件下煅烧4h。自然冷却后取出样品研磨成粉末状,得到氮化碳粉末。称取2g氮化碳粉末与286 mg氯化钾加入到10mL水中,搅拌10 min,然后将温度控制在80℃把水蒸干,得到钾离子负载的氮化碳。First, 10 g of melamine was weighed and placed in an alumina crucible, and calcined at 550 °C for 4 h in an air atmosphere. After natural cooling, the sample was taken out and ground into powder to obtain carbon nitride powder. Weigh 2 g of carbon nitride powder and 286 mg of potassium chloride into 10 mL of water, stir for 10 min, and then control the temperature at 80 °C to evaporate the water to dryness to obtain potassium ion-supported carbon nitride.
图1为实施例1所得的离子热法合成钾离子修饰的氮化碳和浸渍法合成钾离子负载的氮化碳的X射线粉末衍射图(XRD), 从图中可以看出离子热法合成碱金属离子修饰的氮化碳中氮化碳的结晶度得到改善。Figure 1 is the X-ray powder diffraction pattern (XRD) of the potassium ion-modified carbon nitride synthesized by the ionothermal method and the potassium ion-supported carbon nitride synthesized by the impregnation method obtained in Example 1. It can be seen from the figure that the ionothermal method is synthesized The crystallinity of carbon nitride in the alkali metal ion modified carbon nitride is improved.
图2为实施例1所得的离子热法合成钾离子修饰的氮化碳和浸渍法合成钾离子负载的氮化碳的傅里叶变换红外光谱图(FT-IR),从图中可以看出在800 cm-1和1200~1600cm-1区间,它们分别对应于嗪环的呼吸振动和芳香性CN杂环伸缩振动,在3200 cm-1区间主要由于纳米层状氮化碳表面存在比较多未键合的NH2、NH所引起的,证实制备的产物为氮化碳材料。Fig. 2 is the Fourier transform infrared spectrogram (FT-IR) of the ionothermal synthesis of potassium ion-modified carbon nitride obtained in Example 1 and the synthesis of potassium ion-supported carbon nitride by impregnation method, as can be seen from the figure In the range of 800 cm -1 and 1200~1600 cm -1 , they correspond to the breathing vibration of the oxazine ring and the stretching vibration of the aromatic CN heterocycle, respectively . Caused by the bonded NH 2 , NH, it was confirmed that the prepared product was a carbon nitride material.
图3为实施例1所得的钾离子修饰的氮化碳的高分辨透射电镜图(TEM)和mapping图,从图中可以看到明显的晶格条纹,晶格条纹间距为0 .31nm。从mapping图中可以看出钾离子分布均匀。3 is a high-resolution transmission electron microscope (TEM) and mapping image of the potassium ion-modified carbon nitride obtained in Example 1. From the figure, obvious lattice fringes can be seen, and the lattice fringe spacing is 0.31 nm. It can be seen from the mapping diagram that potassium ions are distributed uniformly.
图4为实施例1所合成的钾离子修饰的氮化碳催化COS水解的活性图,从图中我们可以得出采用浸渍法合成的钾离子负载的氮化碳基本没有催化COS水解的活性,而用离子热法合成的钾离子修饰的氮化碳具有较高的COS水解催化活性,在10小时的催化反应中,COS转化率达到92%,且活性未发生明显变化,稳定性好。Figure 4 is the activity diagram of the potassium ion-modified carbon nitride synthesized in Example 1 to catalyze the hydrolysis of COS. From the figure, we can draw that the potassium ion-supported carbon nitride synthesized by the impregnation method has basically no activity to catalyze the hydrolysis of COS, The potassium ion-modified carbon nitride synthesized by ionothermal method has high catalytic activity for COS hydrolysis. In the catalytic reaction for 10 hours, the COS conversion rate reaches 92%, and the activity does not change significantly, and the stability is good.
以上所述仅为本发明的较佳实施例,凡依本发明申请专利范围所做的均等变化与修饰,皆应属本发明的涵盖范围。The above descriptions are only preferred embodiments of the present invention, and all equivalent changes and modifications made according to the scope of the patent application of the present invention shall fall within the scope of the present invention.
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