CN114768852A - Preparation method of potassium ion gradient doped carbon nitride material - Google Patents
Preparation method of potassium ion gradient doped carbon nitride material Download PDFInfo
- Publication number
- CN114768852A CN114768852A CN202210422019.XA CN202210422019A CN114768852A CN 114768852 A CN114768852 A CN 114768852A CN 202210422019 A CN202210422019 A CN 202210422019A CN 114768852 A CN114768852 A CN 114768852A
- Authority
- CN
- China
- Prior art keywords
- potassium
- carbon nitride
- pcn
- potassium ion
- temperature
- 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.)
- Granted
Links
- 229910001414 potassium ion Inorganic materials 0.000 title claims abstract description 56
- NPYPAHLBTDXSSS-UHFFFAOYSA-N Potassium ion Chemical compound [K+] NPYPAHLBTDXSSS-UHFFFAOYSA-N 0.000 title claims abstract description 33
- JMANVNJQNLATNU-UHFFFAOYSA-N oxalonitrile Chemical compound N#CC#N JMANVNJQNLATNU-UHFFFAOYSA-N 0.000 title claims abstract description 33
- 239000000463 material Substances 0.000 title claims abstract description 32
- 238000002360 preparation method Methods 0.000 title claims abstract description 19
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 claims abstract description 96
- 238000000034 method Methods 0.000 claims abstract description 21
- 229910052700 potassium Inorganic materials 0.000 claims abstract description 21
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 claims abstract description 18
- 238000001354 calcination Methods 0.000 claims abstract description 18
- 239000011591 potassium Substances 0.000 claims abstract description 18
- 238000002156 mixing Methods 0.000 claims abstract description 17
- BPUBBGLMJRNUCC-UHFFFAOYSA-N oxygen(2-);tantalum(5+) Chemical compound [O-2].[O-2].[O-2].[O-2].[O-2].[Ta+5].[Ta+5] BPUBBGLMJRNUCC-UHFFFAOYSA-N 0.000 claims abstract description 15
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 claims abstract description 14
- 239000004202 carbamide Substances 0.000 claims abstract description 14
- 229910001936 tantalum oxide Inorganic materials 0.000 claims abstract description 6
- 239000007787 solid Substances 0.000 claims description 91
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 45
- 239000001257 hydrogen Substances 0.000 claims description 44
- 229910052739 hydrogen Inorganic materials 0.000 claims description 44
- 239000000843 powder Substances 0.000 claims description 44
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 42
- 238000004519 manufacturing process Methods 0.000 claims description 31
- 238000010438 heat treatment Methods 0.000 claims description 20
- 230000001699 photocatalysis Effects 0.000 claims description 19
- 238000006243 chemical reaction Methods 0.000 claims description 17
- 239000000725 suspension Substances 0.000 claims description 13
- 238000007789 sealing Methods 0.000 claims description 11
- 238000002425 crystallisation Methods 0.000 claims description 6
- 230000008025 crystallization Effects 0.000 claims description 6
- 239000002243 precursor Substances 0.000 claims description 6
- 238000000354 decomposition reaction Methods 0.000 claims description 4
- 229920000877 Melamine resin Polymers 0.000 claims description 2
- JDSHMPZPIAZGSV-UHFFFAOYSA-N melamine Chemical compound NC1=NC(N)=NC(N)=N1 JDSHMPZPIAZGSV-UHFFFAOYSA-N 0.000 claims description 2
- 238000009826 distribution Methods 0.000 abstract description 19
- 238000011065 in-situ storage Methods 0.000 abstract description 13
- 238000000227 grinding Methods 0.000 abstract description 12
- 150000002500 ions Chemical class 0.000 abstract description 11
- 238000009792 diffusion process Methods 0.000 abstract description 10
- 239000000969 carrier Substances 0.000 abstract description 6
- 230000007547 defect Effects 0.000 abstract description 4
- 229920000642 polymer Polymers 0.000 abstract description 3
- 239000000758 substrate Substances 0.000 abstract description 3
- 239000002648 laminated material Substances 0.000 abstract description 2
- 239000003054 catalyst Substances 0.000 abstract 1
- 230000005012 migration Effects 0.000 abstract 1
- 238000013508 migration Methods 0.000 abstract 1
- 239000011232 storage material Substances 0.000 abstract 1
- 230000002194 synthesizing effect Effects 0.000 abstract 1
- 239000000203 mixture Substances 0.000 description 40
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 33
- 230000000052 comparative effect Effects 0.000 description 24
- 239000002245 particle Substances 0.000 description 23
- 230000000694 effects Effects 0.000 description 21
- 238000001035 drying Methods 0.000 description 20
- 238000005406 washing Methods 0.000 description 20
- 239000000919 ceramic Substances 0.000 description 14
- 239000007789 gas Substances 0.000 description 13
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 description 12
- RZVAJINKPMORJF-UHFFFAOYSA-N Acetaminophen Chemical compound CC(=O)NC1=CC=C(O)C=C1 RZVAJINKPMORJF-UHFFFAOYSA-N 0.000 description 11
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 11
- 239000002253 acid Substances 0.000 description 11
- 239000007864 aqueous solution Substances 0.000 description 11
- 239000003795 chemical substances by application Substances 0.000 description 11
- 239000008367 deionised water Substances 0.000 description 11
- 229910021641 deionized water Inorganic materials 0.000 description 11
- 238000000151 deposition Methods 0.000 description 11
- 230000008021 deposition Effects 0.000 description 11
- 238000001914 filtration Methods 0.000 description 11
- 239000011521 glass Substances 0.000 description 11
- 239000004570 mortar (masonry) Substances 0.000 description 11
- 238000013032 photocatalytic reaction Methods 0.000 description 11
- 239000005297 pyrex Substances 0.000 description 11
- 239000000243 solution Substances 0.000 description 11
- 238000003756 stirring Methods 0.000 description 11
- 238000012360 testing method Methods 0.000 description 11
- 229910052724 xenon Inorganic materials 0.000 description 11
- FHNFHKCVQCLJFQ-UHFFFAOYSA-N xenon atom Chemical compound [Xe] FHNFHKCVQCLJFQ-UHFFFAOYSA-N 0.000 description 11
- 238000010586 diagram Methods 0.000 description 10
- 238000005303 weighing Methods 0.000 description 10
- 239000003513 alkali Substances 0.000 description 9
- 239000012298 atmosphere Substances 0.000 description 9
- 239000006228 supernatant Substances 0.000 description 9
- PBCFLUZVCVVTBY-UHFFFAOYSA-N tantalum pentoxide Inorganic materials O=[Ta](=O)O[Ta](=O)=O PBCFLUZVCVVTBY-UHFFFAOYSA-N 0.000 description 9
- 238000009210 therapy by ultrasound Methods 0.000 description 9
- -1 polytetrafluoroethylene Polymers 0.000 description 8
- 229920001343 polytetrafluoroethylene Polymers 0.000 description 8
- 239000004810 polytetrafluoroethylene Substances 0.000 description 8
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 7
- 238000012876 topography Methods 0.000 description 7
- 239000013078 crystal Substances 0.000 description 6
- 238000012986 modification Methods 0.000 description 6
- 230000004048 modification Effects 0.000 description 6
- 230000001678 irradiating effect Effects 0.000 description 5
- 238000011068 loading method Methods 0.000 description 5
- 239000000047 product Substances 0.000 description 5
- 239000004065 semiconductor Substances 0.000 description 5
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 4
- 229910052799 carbon Inorganic materials 0.000 description 4
- 229910052757 nitrogen Inorganic materials 0.000 description 4
- 229910002804 graphite Inorganic materials 0.000 description 3
- 239000010439 graphite Substances 0.000 description 3
- 238000002173 high-resolution transmission electron microscopy Methods 0.000 description 3
- 230000006798 recombination Effects 0.000 description 3
- 238000005215 recombination Methods 0.000 description 3
- 238000000926 separation method Methods 0.000 description 3
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- ZOXJGFHDIHLPTG-UHFFFAOYSA-N Boron Chemical group [B] ZOXJGFHDIHLPTG-UHFFFAOYSA-N 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 238000006555 catalytic reaction Methods 0.000 description 2
- 239000002131 composite material Substances 0.000 description 2
- 238000005265 energy consumption Methods 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 239000002135 nanosheet Substances 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- 239000011941 photocatalyst Substances 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 238000004544 sputter deposition Methods 0.000 description 2
- 238000003786 synthesis reaction Methods 0.000 description 2
- 229910052715 tantalum Inorganic materials 0.000 description 2
- 239000010409 thin film Substances 0.000 description 2
- 239000004408 titanium dioxide Substances 0.000 description 2
- WUPHOULIZUERAE-UHFFFAOYSA-N 3-(oxolan-2-yl)propanoic acid Chemical compound OC(=O)CCC1CCCO1 WUPHOULIZUERAE-UHFFFAOYSA-N 0.000 description 1
- JLVVSXFLKOJNIY-UHFFFAOYSA-N Magnesium ion Chemical compound [Mg+2] JLVVSXFLKOJNIY-UHFFFAOYSA-N 0.000 description 1
- ZOKXTWBITQBERF-UHFFFAOYSA-N Molybdenum Chemical compound [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 description 1
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- 239000004809 Teflon Substances 0.000 description 1
- 229920006362 Teflon® Polymers 0.000 description 1
- 229910052786 argon Inorganic materials 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 238000000498 ball milling Methods 0.000 description 1
- 238000005452 bending Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 229910052797 bismuth Inorganic materials 0.000 description 1
- JCXGWMGPZLAOME-UHFFFAOYSA-N bismuth atom Chemical compound [Bi] JCXGWMGPZLAOME-UHFFFAOYSA-N 0.000 description 1
- 229910052796 boron Inorganic materials 0.000 description 1
- 229910052980 cadmium sulfide Inorganic materials 0.000 description 1
- 238000005119 centrifugation Methods 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 230000007646 directional migration Effects 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 230000005684 electric field Effects 0.000 description 1
- 238000005868 electrolysis reaction Methods 0.000 description 1
- 238000004146 energy storage Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000005530 etching Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 239000002803 fossil fuel Substances 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 229910021389 graphene Inorganic materials 0.000 description 1
- 230000000977 initiatory effect Effects 0.000 description 1
- 229910052746 lanthanum Inorganic materials 0.000 description 1
- FZLIPJUXYLNCLC-UHFFFAOYSA-N lanthanum atom Chemical compound [La] FZLIPJUXYLNCLC-UHFFFAOYSA-N 0.000 description 1
- 230000004298 light response Effects 0.000 description 1
- 238000013332 literature search Methods 0.000 description 1
- 229910001425 magnesium ion Inorganic materials 0.000 description 1
- 229910052750 molybdenum Inorganic materials 0.000 description 1
- 239000011733 molybdenum Substances 0.000 description 1
- 239000002073 nanorod Substances 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 230000004044 response Effects 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 229910052703 rhodium Inorganic materials 0.000 description 1
- 239000010948 rhodium Substances 0.000 description 1
- MHOVAHRLVXNVSD-UHFFFAOYSA-N rhodium atom Chemical compound [Rh] MHOVAHRLVXNVSD-UHFFFAOYSA-N 0.000 description 1
- 230000003595 spectral effect Effects 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- VEALVRVVWBQVSL-UHFFFAOYSA-N strontium titanate Chemical compound [Sr+2].[O-][Ti]([O-])=O VEALVRVVWBQVSL-UHFFFAOYSA-N 0.000 description 1
- 230000009897 systematic effect Effects 0.000 description 1
- MZLGASXMSKOWSE-UHFFFAOYSA-N tantalum nitride Chemical compound [Ta]#N MZLGASXMSKOWSE-UHFFFAOYSA-N 0.000 description 1
- 238000002303 thermal reforming Methods 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
- WFKWXMTUELFFGS-UHFFFAOYSA-N tungsten Chemical compound [W] WFKWXMTUELFFGS-UHFFFAOYSA-N 0.000 description 1
- 239000010937 tungsten Substances 0.000 description 1
- 229910052721 tungsten Inorganic materials 0.000 description 1
- 238000001132 ultrasonic dispersion Methods 0.000 description 1
- LSGOVYNHVSXFFJ-UHFFFAOYSA-N vanadate(3-) Chemical compound [O-][V]([O-])([O-])=O LSGOVYNHVSXFFJ-UHFFFAOYSA-N 0.000 description 1
Images
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
- 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
- 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
- B01J35/30—Catalysts, in general, characterised by their form or physical properties characterised by their physical properties
- B01J35/39—Photocatalytic properties
-
- 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
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/08—Heat treatment
- B01J37/082—Decomposition and pyrolysis
-
- 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
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/08—Heat treatment
- B01J37/10—Heat treatment in the presence of water, e.g. steam
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
- C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
- C01B3/04—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by decomposition of inorganic compounds, e.g. ammonia
- C01B3/042—Decomposition of water
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/36—Hydrogen production from non-carbon containing sources, e.g. by water electrolysis
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Health & Medical Sciences (AREA)
- General Health & Medical Sciences (AREA)
- Combustion & Propulsion (AREA)
- Inorganic Chemistry (AREA)
- Catalysts (AREA)
Abstract
The invention relates to a preparation method of a potassium ion gradient doped carbon nitride material. The invention discloses a preparation method and application of a two-dimensional material for realizing gradient doping by using ion diffusion, and discloses a method for realizing gradient doping on the two-dimensional material by introducing an ion storage material as a doping source and performing ion diffusion action and application of the method. The doping source used in the invention is defect pyrochlore type potassium tantalate: tantalum oxide is uniformly dispersed in 6-12mol/L potassium hydroxide solution, and is calcined and synthesized at the temperature of 400-800 ℃ after hydrothermal alkalization at the temperature of 120-180 ℃. The two-dimensional substrate material used is a polymer carbon nitride laminated material: grinding and mixing potassium tantalate and urea, and calcining and synthesizing at the temperature of 400-600 ℃ under a closed condition. The catalyst prepared by the invention realizes gradient doping distribution of potassium ions constructed in situ on graphite-phase carbon nitride, enhances the migration of photon-generated carriers and further improves the photo-and photo-electro-catalytic properties.
Description
Technical Field
The invention belongs to the technical field of catalysis, particularly relates to a preparation method of a potassium ion gradient doped carbon nitride material, and particularly relates to a preparation method and application of a potassium ion radiation gradient doped polymer carbon nitride material guided by ion diffusion behavior.
Background
The increasing global energy consumption has caused extensive and intensive attention to the problems of resource sustainable utilization and environmental protection. The hydrogen energy with the characteristics of energy storage and zero carbon is considered to be an eco-friendly renewable clean energy with great potential and is an ideal substitute for the traditional fossil fuel. The traditional hydrogen production methods such as a water gas method, a methane steam thermal reforming method and a water electrolysis method relying on traditional electric power all have the problems of energy consumption and pollution. Therefore, the light/photoelectrocatalysis technology directly utilizing solar energy is more and more concerned and researched especially in the field of hydrogen production by water decomposition, and the solar water-saving hydrogen production device has wide application prospect.
In 1972, Japanese scientists Fujishima and Honda discovered that biased titanium dioxide electrodes decomposed water under ultraviolet light to produce hydrogen gas (Nature,1972,238(5358):37-38), whereby the Fujishima-Honda effect opened up the sequential screen for hydrogen production by artificial photocatalytic decomposition of water. In the systematic study of semiconductor photocatalytic powder systems, the problem of separation of photogenerated electron-hole pairs is considered to be a major obstacle limiting the access to efficient solar energy conversion to hydrogen. In a classical semiconductor material, the concentration level of carriers in the semiconductor can be effectively adjusted by doping different atoms, so that the purposes of adjusting a proper energy band structure and band gap width and improving the separation capability of the carriers are achieved. For titanium dioxide photocatalytic materials, the valence band composition is adjusted by nitrogen doping and the visible light response capability is given (Nano letters,2003,3(8): 1049-. For strontium titanate photocatalytic Materials, lanthanum and rhodium doping introduces electron reconstruction to greatly improve carrier lifetime (Nature Materials,2021,20(4):511-3+The defect density increases The oxygen vacancy content to suppress The intrinsic carrier recombination problem (The Journal of Physical Chemistry C,2009,113(45): 19386-. For visible light responding bismuth vanadate photocatalytic materials, tungsten and molybdenum doping introduces shallow impurity energy levels so as to promote the transfer efficiency of carriers (ChemSusChem,2012,5(10): 1926-. Compared with the traditional uniform doping, the gradient concentration doping can continuously regulate and control the bending of an energy band, and is beneficial to the directional migration of current carriers so as to inhibit the current carriersThe recombination of the molecules has become a hot research point in the modification of semiconductors in recent years. Xiao et al report that magnesium ion gradient doping realizes high-performance photoelectrocatalytic water oxidation efficiency by band design and defect regulation of a tantalum nitride photo-anode (Nature Catalysis,2020,3(11): 932-. Huang et al reported that a directional built-in electric field is constructed by phosphorus gradient doped cadmium sulfide nanorods to realize efficient separation of photogenerated carriers from bulk phase to surface (Nano letters,2017,17(6): 3803-.
The literature search of the prior art finds that Chinese invention patent with application publication number CN 110240133A, namely 'potassium ion doped graphite phase carbon nitride nanosheet photocatalyst and a preparation method thereof', discloses a uniform potassium ion doped graphite phase carbon nitride nanosheet photocatalyst and an equipment method thereof, and widens the spectral response range so as to enhance the photocatalytic activity. However, the ball milling method and the air oxidation etching method cannot control the doping distribution of potassium ions, and the modified carbon nitride skeleton structure has a stability problem.
The document retrieval of the prior art finds that the Chinese patent with the application publication number of CN 112626470A, namely 'a preparation method of a CN thin film with self-doping carbon and gradient distribution of concentration', discloses a preparation method of a CN thin film with gradient concentration of carbon content, and is used for designing and utilizing electronic elements. But the ion sputtering coating process and the bombardment of N by argon gas2As N+The ion source has the defects of complicated preparation process, expensive equipment and unsuitability for large-scale popularization and application.
The document retrieval of the prior art finds that the Chinese patent with the application publication number of CN 109835892A, namely 'a preparation method of boron-doped semiconductor graphite', discloses that boron atoms are released by a boron source at high temperature to form substitutional doped graphene. However, the synthesis temperature (2000-.
Disclosure of Invention
The invention aims to provide a preparation method of a potassium ion gradient doped carbon nitride material aiming at the problems in the prior art, and particularly relates to a preparation method for realizing a gradient doped two-dimensional material by using ion diffusion and application thereof.
The invention provides a two-dimensional material gradient doping method with low cost and simple process, which is characterized in that a particle source (defective pyrochlore potassium tantalate) with ion storage and release capacity is used as a potassium ion doping source, a classical Polymer Carbon Nitride (PCN) two-dimensional material is used as a substrate, and a potassium ion doping modified PCN (marked as (K) PCN & KTO) is obtained in an ion diffusion mode and presents radial potassium ion concentration gradient distribution.
The purpose of the invention can be realized by the following scheme:
in a first aspect, the invention provides a preparation method of a potassium ion gradient doped carbon nitride material, which specifically comprises the following steps:
s1, mixing the tantalum oxide powder with a potassium hydroxide solution to obtain a white suspension, heating for reaction, and centrifuging to obtain a white solid;
s2, calcining and crystallizing the white solid to obtain pyrochlore potassium tantalate (KTO) as a potassium ion sourcepyr) A solid powder;
s3, adding potassium ion source potassium tantalate (KTO)pyr) And mixing the solid powder with the carbon nitride precursor, sealing and heating to obtain the potassium ion gradient doped carbon nitride material.
As an embodiment of the present invention, the concentration of potassium hydroxide in step S1 is 6mol/L to 12 mol/L. The dosage ratio of the potassium hydroxide solution to the tantalum oxide is 100 mL: 5-8 g.
As an embodiment of the present invention, the mixing in step S1 is mixing by ultrasonic dispersion treatment. After dispersion, the mixture was further stirred to obtain a uniformly dispersed white suspension.
As an embodiment of the invention, the temperature of the heating reaction in the step S1 is 120-180 ℃, and the heating time is 6-12 h. The heating reaction is carried out in a hydrothermal kettle. The product of the centrifugation of the suspension was washed and dried to give a white solid. Too high or too low of the reaction temperature can affect the crystal form of a hydrothermal product, too low can form tantalum oxide impurities, and too high can form perovskite potassium tantalate.
As an embodiment of the invention, the temperature of the calcination crystallization in the step S2 is 400-800 ℃, and the time of the calcination crystallization is 6-12 h. The calcination is carried out under an air atmosphere. The crystallization temperature is too low, the crystallinity is poor, and the crystal structure is unstable; too high a crystallization temperature tends to cause transformation of the crystal form into the perovskite form.
As one embodiment of the present invention, the mixing in step S3 is mill mixing. The sealing is performed by using tin foil paper, and the calcination is performed in a ceramic crucible.
As one embodiment of the present invention, the mass of the potassium tantalate solid powder as the potassium ion source used in step S3 is 0.5% to 10% of the mass of the carbon nitride precursor. The gradient doping is formed by utilizing the slow release of potassium tantalate ions.
As an embodiment of the present invention, the carbon nitride precursor includes one of urea and melamine.
As an embodiment of the present invention, the heating temperature in the step S3 is 500 ℃ to 600 ℃, and the heating time is 3h to 6 h. The heating rate is 1-3 deg.C/min. When the temperature is too high, carbon nitride cannot be obtained, and when the temperature is too low, the crystallinity is poor. Too fast or too slow a temperature increase rate may affect the crystallinity and initial activity of the carbon nitride.
As an embodiment of the invention, the heating product is fully ground in the step S3, and is washed by water, dried and ground to obtain the potassium ion gradient doped carbon nitride material. The obtained carbon nitride material is PCN doped with potassium ions in a gradient manner and containing a particle doping source.
In a second aspect, the invention also provides an application of the potassium ion gradient doped carbon nitride material in the field of hydrogen production by photocatalytic water decomposition.
The invention introduces pyrochlore type K2Ta2O6(abbreviated as KTO)pyr) As a potassium ion doping source, potassium ion concentration gradient distribution is constructed in situ on the carbon nitride laminated material through potassium ion diffusion behavior.
Compared with the prior art, the invention has the following promotion effects:
(1) compared with the processes such as ion evaporation sputtering and the like, the two-dimensional gradient doping method has the advantages of economy, simplicity, low price and easy obtainment of used raw materials, and certain universality for doping modification of two-dimensional materials.
(2) Compared with the traditional modified PCN uniformly doped with potassium ions and the blank unmodified PCN, the modified PCN doped with potassium ions in a gradient manner is obviously improved in the aspect of photo/photoelectrocatalysis performance, and the problem of serious carrier recombination of the original PCN material is solved, so that the hydrogen production efficiency by decomposing water is improved.
Drawings
The main advantages and other features of the invention are demonstrated by reading the detailed description of a non-limiting embodiment with reference to the following figures:
FIG. 1 shows KTO in example 1pyrThe morphology of octahedral particles, a and b are KTO in example 1pyrSEM topography of octahedral particles; c is KTO from example 1pyrTEM topography of octahedral particles;
FIG. 2 is the morphology diagrams of (K) PCN & KTO in example 1, and a and b are SEM morphology diagrams of (K) PCN & KTO in example 1; c is the TEM topography of (K) PCN & KTO of example 1;
FIG. 3 is KTO of comparative example 1perMorphology of cubic particles, a is KTO in comparative example 1perSEM topography of cubic particles; b. c is KTO in comparative example 1perTEM topography of cubic particles;
FIG. 4 shows (K) PCN in comparative example 1&KTOperA TEM topography of (a);
FIG. 5 is a TEM morphology of (K) PCN & KOH in comparative example 2;
FIG. 6 is a morphology view of a blank PCN in comparative example 3, a is an SEM morphology view of a blank PCN in comparative example 3; b is the TEM topography of the blank PCN in comparative example 3.
FIG. 7 is a bright field map, an EDS map, relative contents of elements, and a K/N atomic ratio distribution map of (K) PCN & KTO of example 1, and a is a bright field map of (K) PCN & KTO of example 1; b. c and d are EDS (element distribution) graphs (corresponding to K, Ta and N elements respectively) of PCN & KTO in example 1, and the scale bars are all 200 nm; e. f is a distribution graph of the relative contents of the elements and the K/N atomic ratio of (K) PCN & KTO along the Line # 1 and the Line # 2 in example 1.
FIG. 8 shows (K) PCN of comparative example 1&KTOperA is a distribution diagram of (K) PCN in comparative example 1, a is a bright field diagram, an EDS diagram, a relative element content and a K/N atomic ratio&KTOperBright field map of (a); b. c, d are (K) PCN in comparative example 1&KTOperEDS (element distribution) chart (corresponding to K, Ta and N elements respectively) of (1), wherein the scale bar is 200 nm; e. f is (K) PCN in comparative example 1&KTOperThe distribution of the relative contents of elements and the K/N atomic ratios along the Line # 1 and the Line # 2.
FIG. 9 is a bright field diagram, an EDS diagram, relative contents of elements, and a K/N atomic ratio distribution diagram of (K) PCN & KOH of comparative example 2, and a is a bright field diagram of (K) PCN & KOH of comparative example 2; b. c and d are EDS diagrams (corresponding to K, C, N elements respectively) of element distribution of (K) PCN & KOH in comparative example 2, and the scale bars are both 200 nm; e. f is a distribution graph of the relative contents of the elements (K) PCN & KOH and the K/N atomic ratio along the Line # 1 and the Line # 2 in the comparative example 2.
Detailed Description
The present invention is described in detail below with reference to the accompanying drawings and specific embodiments, and the following examples are implemented under the guidance of the technical solution of the present invention, and provide detailed implementation methods and specific operation procedures, which will help those skilled in the art to further understand the technical solution of the present invention. It should be noted that the protection scope of the present invention is not limited to the following embodiments, and several modifications and improvements made on the premise of the idea of the present invention belong to the protection scope of the present invention.
Example 1
1. Dissolving 48g of potassium hydroxide solid in 100mL of pure water, fully stirring to obtain a potassium hydroxide solution, adding 5g of tantalum (V) oxide, performing ultrasonic treatment for 10min, and stirring to obtain a uniformly dispersed white suspension.
2. The solution is transferred to a 100mL polytetrafluoroethylene lining and then placed in a hydrothermal kettle to be heated in an oven at 160 ℃ for 8 h.
3. Separating the white solid powder after the hydrothermal alkalization reaction from the supernatant alkali liquor, centrifugally washing the white solid powder for 5 times until the pH value of the centrifugate is 7, and then placing the centrifugally treated solid in a vacuum oven at 80 ℃ for overnight drying.
4. The dried white powder was thoroughly ground and calcined in an air atmosphere at 600 ℃ for 10 h.
5. And (3) putting 0.5g of calcined white powder and 20g of urea into an agate mortar for full mixing, transferring the mixture into a ceramic crucible, sealing the mixture by using 4 layers of tinfoil paper, putting the mixture into a muffle furnace, heating the mixture to 550 ℃ at the speed of 2.5 ℃/min, and calcining the mixture for 2 hours at the temperature to obtain a yellow honeycomb-shaped solid.
6. And fully grinding the yellow solid, filtering and washing the ground yellow solid by using deionized water, and then placing the washed yellow solid in a vacuum oven at 80 ℃ for overnight drying to obtain the PCN doped with potassium ions in a gradient manner, wherein the mark is (K) PCN & KTO (600) -2.5-2 h.
7. Weighing 50mg (K) PCN&Ultrasonically dispersing a KTO (600) -2.5-2H sample in 80mL of pure water, adding 20mL of methanol serving as a sacrificial agent, and adding 37mL of chloroplatinic acid (H)2PtCl6) The aqueous solution (1.48mgPt/mL) is placed in a Pyrex glass photocatalytic reactor, a 300W xenon lamp is used as a light source, the Pt promoter is firstly irradiated for 2h in-situ light deposition loading under a visible light wave band (more than or equal to 420nm), and then hydrogen production activity test is carried out every hour. The hydrogen generated by the photocatalytic reaction is quantitatively sampled and analyzed by a gas chromatograph with a thermal conductivity detector, and the average hydrogen production rate is 20.4 mu mol/h.
As shown in figure 1, KTO prepared by hydrothermal alkalizationpyrHas an octahedral structure typical of pyrochlore crystal forms.
KTO as shown in FIG. 2pyrGood composite contact is formed between the particles and the layered PCN.
As shown in FIG. 7, with KTOpyr(K) PCN with particles doped as a source of potassium ions&The KTO samples exhibited efficient potassium doping. Elemental distribution display of high resolution TEM as KTOpyrThe particle is taken as a source, the K/N atomic ratio shows a radial gradient descending trend along the Line # 1, and the non-gradient distribution along the Line # 2 shows that KTO is distributedpyrIon diffusion doping does not occur without effective contact of the particles with the PCN substrate.
Example 2
1.48 g of potassium hydroxide solid is dissolved in 100mL of pure water and fully stirred to obtain a potassium hydroxide solution, 5g of tantalum (V) oxide is added, and then ultrasonic treatment is carried out for 10min and stirring is carried out to obtain a uniform white suspension.
2. The solution is transferred to a 100mL polytetrafluoroethylene lining and then placed in a hydrothermal kettle to be heated in an oven at 160 ℃ for 8 hours.
3. Separating the white solid powder after the hydrothermal alkalization reaction from the supernatant alkali liquor, centrifugally washing the white solid powder for 5 times until the pH value of the centrifugate is 7, and then placing the centrifugally treated solid in a vacuum oven at 80 ℃ for overnight drying.
4. The dried white powder was thoroughly ground and calcined in an air atmosphere at 600 ℃ for 10 h.
5. And (3) putting 0.5g of calcined white powder and 20g of urea into an agate mortar for full mixing, transferring the mixture into a ceramic crucible, sealing the mixture by using 4 layers of tinfoil paper, putting the mixture into a muffle furnace, heating the mixture to 550 ℃ at the speed of 2.5 ℃/min, and calcining the mixture for 4 hours at the temperature to obtain a yellow honeycomb-shaped solid.
6. And (3) fully grinding the yellow solid, filtering and washing the ground yellow solid by using deionized water, and then placing the washed yellow solid in a vacuum oven at 80 ℃ for overnight drying to obtain the PCN doped with potassium ions in a gradient manner, wherein the PCN is marked as (K) PCN & KTO (600) -2.5-4 h.
7. Weighing 50mg (K) PCN&Ultrasonically dispersing a KTO (600) -2.5-4H sample in 80mL of pure water, adding 20mL of methanol serving as a sacrificial agent, and adding 37mL of chloroplatinic acid (H)2PtCl6) The aqueous solution (1.48mgPt/mL) is placed in a Pyrex glass photocatalytic reactor, a 300W xenon lamp is used as a light source, the Pt promoter is firstly irradiated for 2h in-situ light deposition loading under a visible light wave band (more than or equal to 420nm), and then hydrogen production activity test is carried out every hour. The hydrogen produced by the photocatalytic reaction is quantitatively sampled and analyzed by a gas chromatograph with a thermal conductivity detector, and the average hydrogen production rate is 24.6 mu mol/h.
Example 3
1.48 g of potassium hydroxide solid is dissolved in 100mL of pure water and fully stirred to obtain a potassium hydroxide solution, 5g of tantalum (V) oxide is added, and then ultrasonic treatment is carried out for 10min and stirring is carried out to obtain a uniform white suspension.
2. The solution is transferred to a 100mL polytetrafluoroethylene lining and then placed in a hydrothermal kettle to be heated in an oven at 160 ℃ for 8 hours.
3. Separating the white solid powder after the hydrothermal alkalization reaction from the supernatant alkali liquor, centrifugally washing the white solid powder for 5 times until the pH value of the centrifugate is 7, and then placing the centrifugally treated solid in a vacuum oven at 80 ℃ for overnight drying.
4. The dried white powder was thoroughly ground and calcined in an air atmosphere at 600 ℃ for 10 h.
5. And (3) putting 0.5g of calcined white powder and 20g of urea into an agate mortar for full mixing, transferring the mixture into a ceramic crucible, sealing the mixture by using 4 layers of tinfoil paper, putting the mixture into a muffle furnace, heating the mixture to 550 ℃ at the speed of 2.5 ℃/min, and calcining the mixture for 6 hours at the temperature to obtain a yellow honeycomb-shaped solid.
6. And fully grinding the yellow solid, filtering and washing the ground yellow solid by using deionized water, and then placing the washed yellow solid in a vacuum oven at 80 ℃ for overnight drying to obtain the PCN (K) with gradient doping of potassium ions, wherein the mark is (K) PCN & KTO (600) -2.5-8 h.
7. Weighing 50mg (K) PCN&Ultrasonically dispersing a KTO (600) -2.5-8H sample in 80mL of pure water, adding 20mL of methanol serving as a sacrificial agent, and adding 37mL of chloroplatinic acid (H)2PtCl6) The aqueous solution (1.48mgPt/mL) is placed in a Pyrex glass photocatalytic reactor, a 300W xenon lamp is used as a light source, the Pt promoter is loaded by irradiating for 2h of in-situ light deposition under a visible light wave band (not less than 420nm), and then the hydrogen production activity test is carried out every hour. The hydrogen generated by the photocatalytic reaction is quantitatively sampled and analyzed by a gas chromatograph with a thermal conductivity detector, and the average hydrogen production rate is 20.3 mu mol/h.
Example 4
1.48 g of potassium hydroxide solid is dissolved in 100mL of pure water and fully stirred to obtain a potassium hydroxide solution, 5g of tantalum (V) oxide is added, and then ultrasonic treatment is carried out for 10min and stirring is carried out to obtain a uniform white suspension.
2. The solution is transferred to a 100mL polytetrafluoroethylene lining and then placed in a hydrothermal kettle to be heated in an oven at 160 ℃ for 8 hours.
3. Separating the white solid powder after the hydrothermal alkalization reaction from the supernatant alkali liquor, centrifugally washing the white solid powder for 5 times until the pH value of the centrifugate is 7, and then placing the centrifugally treated solid in a vacuum oven at 80 ℃ for overnight drying.
4. 0.5g of white powder and 20g of urea are placed in an agate mortar and are fully mixed, then the mixture is transferred into a ceramic crucible and is sealed by 4 layers of tinfoil paper, the mixture is placed in a muffle furnace, the temperature is raised to 550 ℃ at the speed of 1.5 ℃/min, and the mixture is calcined for 4 hours at the temperature to obtain yellow honeycomb-shaped solid.
5. And (3) fully grinding the yellow solid, filtering and washing the yellow solid by using deionized water, and then placing the yellow solid in a vacuum oven at 80 ℃ for overnight drying to obtain the PCN (K) which is doped with potassium ions in a gradient manner and is marked as (K) PCN & KTO-2.5-4 h.
6. Weighing 50mg (K) PCN&The KTO-2.5% sample was ultrasonically dispersed in 80mL of pure water, 20mL of methanol was added as a sacrificial agent, and 37mL of chloroplatinic acid (H) was added2PtCl6) The aqueous solution (1.48mgPt/mL) is placed in a Pyrex glass photocatalytic reactor, a 300W xenon lamp is used as a light source, the Pt promoter is loaded by irradiating for 2h of in-situ light deposition under a visible light wave band (not less than 420nm), and then the hydrogen production activity test is carried out every hour. The hydrogen generated by the photocatalytic reaction is quantitatively sampled and analyzed by a gas chromatograph with a thermal conductivity detector, and the average hydrogen production rate is 13.3 mu mol/h.
Example 5
1.48 g of potassium hydroxide solid is dissolved in 100mL of pure water and fully stirred to obtain a potassium hydroxide solution, 5g of tantalum (V) oxide is added, and then ultrasonic treatment is carried out for 10min and stirring is carried out to obtain a uniform white suspension.
2. The solution is transferred to a 100mL polytetrafluoroethylene lining and then placed in a hydrothermal kettle to be heated in an oven at 160 ℃ for 8 h.
3. Separating the white solid powder after the hydrothermal alkalization reaction from the supernatant alkali liquor, centrifugally washing the white solid powder for 5 times until the pH value of the centrifugate is 7, and then placing the centrifugally treated solid in a vacuum oven at 80 ℃ for overnight drying.
4. The dried white powder was thoroughly ground and calcined in an air atmosphere at 800 ℃ for 10 h.
5. And (3) putting 0.5g of calcined white powder and 20g of urea into an agate mortar for full mixing, transferring the mixture into a ceramic crucible, sealing the mixture by using 4 layers of tinfoil paper, putting the mixture into a muffle furnace, heating the mixture to 550 ℃ at the speed of 2.5 ℃/min, and calcining the mixture for 4 hours at the temperature to obtain a yellow honeycomb-shaped solid.
6. And fully grinding the yellow solid, filtering and washing the ground yellow solid by using deionized water, and then placing the washed yellow solid in a vacuum oven at 80 ℃ for overnight drying to obtain the PCN (K) PCN & KTO (800) -2.5-4 h doped with potassium ions in a gradient manner.
7. Weighing 50mg (K) PCN&Ultrasonically dispersing a KTO (800) -2.5-4H sample in 80mL of pure water, adding 20mL of methanol serving as a sacrificial agent, and adding 37mL of chloroplatinic acid (H)2PtCl6) The aqueous solution (1.48mgPt/mL) is placed in a Pyrex glass photocatalytic reactor, a 300W xenon lamp is used as a light source, the Pt promoter is loaded by irradiating for 2h of in-situ light deposition under a visible light wave band (not less than 420nm), and then the hydrogen production activity test is carried out every hour. The hydrogen generated by the photocatalytic reaction is quantitatively sampled and analyzed by a gas chromatograph with a thermal conductivity detector, and the average hydrogen production rate is 14.8 mu mol/h.
Example 6
1.48 g of potassium hydroxide solid is dissolved in 100mL of pure water and fully stirred to obtain a potassium hydroxide solution, 5g of tantalum (V) oxide is added, and then ultrasonic treatment is carried out for 10min and stirring is carried out to obtain a uniform white suspension.
2. The solution is transferred to a 100mL polytetrafluoroethylene lining and then placed in a hydrothermal kettle to be heated in an oven at 160 ℃ for 8 hours.
3. Separating the white solid powder after the hydrothermal alkalization reaction from the supernatant alkali liquor, centrifugally washing the white solid powder for 5 times until the pH value of the centrifugate is 7, and then placing the centrifugally treated solid in a vacuum oven at 80 ℃ for overnight drying.
4. The dried white powder was thoroughly ground and calcined in an air atmosphere at 600 ℃ for 10 h.
5. Placing 2.0g of calcined white powder and 20g of urea in an agate mortar for fully mixing, transferring the mixture into a ceramic crucible, sealing the ceramic crucible by using 4 layers of tinfoil paper, placing the ceramic crucible in a muffle furnace, raising the temperature to 550 ℃ at the speed of 1.5 ℃/min, and calcining the mixture for 4 hours at the temperature to obtain a yellow honeycomb-shaped solid.
6. And fully grinding the yellow solid, filtering and washing the ground yellow solid by using deionized water, and then placing the washed yellow solid in a vacuum oven at 80 ℃ for overnight drying to obtain the PCN (K) PCN & KTO (600) -10-4 h doped with potassium ions in a gradient manner.
7. Weighing 50mg (K) PCN&Ultrasonically dispersing a KTO (600) -10-4H sample in 80mL of pure water, adding 20mL of methanol serving as a sacrificial agent, and adding 37mL of chloroplatinic acid (H)2PtCl6) The aqueous solution (1.48mgPt/mL) is placed in a Pyrex glass photocatalytic reactor, a 300W xenon lamp is used as a light source, the Pt promoter is loaded by irradiating for 2h of in-situ light deposition under a visible light wave band (not less than 420nm), and then the hydrogen production activity test is carried out every hour. The hydrogen produced by the photocatalytic reaction is quantitatively sampled and analyzed by a gas chromatograph with a thermal conductivity detector, and the average hydrogen production rate is 22.8 mu mol/h.
Example 7
1.48 g of potassium hydroxide solid is dissolved in 100mL of pure water and fully stirred to obtain a potassium hydroxide solution, 5g of tantalum (V) oxide is added, and then ultrasonic treatment is carried out for 10min and stirring is carried out to obtain a uniform white suspension.
2. The solution is transferred to a 100mL polytetrafluoroethylene lining and then placed in a hydrothermal kettle to be heated in an oven at 160 ℃ for 8 hours.
3. Separating the white solid powder after the hydrothermal alkalization reaction from the supernatant alkali liquor, centrifugally washing the white solid powder for 5 times until the pH value of the centrifugate is 7, and then placing the centrifugally treated solid in a vacuum oven at 80 ℃ for overnight drying.
4. The dried white powder was thoroughly ground and calcined in an air atmosphere at a temperature of 700 ℃ for 10 h.
5. And (3) putting 0.5g of calcined white powder and 20g of urea into an agate mortar for full mixing, transferring the mixture into a ceramic crucible, sealing the mixture by using 4 layers of tinfoil paper, putting the mixture into a muffle furnace, heating the mixture to 550 ℃ at the speed of 2.5 ℃/min, and calcining the mixture for 4 hours at the temperature to obtain a yellow honeycomb-shaped solid.
6. And fully grinding the yellow solid, filtering and washing the ground yellow solid by using deionized water, and then placing the washed yellow solid in a vacuum oven at 80 ℃ for overnight drying to obtain the PCN (K) with gradient doping of potassium ions, wherein the mark is (K) PCN & KTO (700) -2.5-4 h.
7. Weighing 50mg (K) PCN&Ultrasonically dispersing a KTO (700) -2.5-4H sample in 80mL of pure water, adding 20mL of methanol serving as a sacrificial agent, and adding 37mL of chloroplatinic acid (H)2PtCl6) The aqueous solution (1.48mgPt/mL) is placed in a Pyrex glass photocatalytic reactor, a 300W xenon lamp is used as a light source, the Pt promoter is firstly irradiated for 2h in-situ light deposition loading under a visible light wave band (more than or equal to 420nm), and then hydrogen production activity test is carried out every hour. The hydrogen generated by the photocatalytic reaction is quantitatively sampled and analyzed by a gas chromatograph with a thermal conductivity detector, and the average hydrogen production rate is 20.4 mu mol/h.
Example 8
1. Dissolving 48g of potassium hydroxide solid in 100mL of pure water, fully stirring to obtain a potassium hydroxide solution, adding 5g of tantalum (V) oxide, performing ultrasonic treatment for 10min, and stirring to obtain a uniformly dispersed white suspension.
2. The solution is transferred to a 100mL polytetrafluoroethylene lining and then placed in a hydrothermal kettle to be heated in an oven at 160 ℃ for 8 h.
3. Separating the white solid powder after the hydrothermal alkalization reaction from the supernatant alkali liquor, centrifugally washing the white solid powder for 5 times until the pH value of the centrifugate is 7, and then placing the centrifugally treated solid in a vacuum oven at 80 ℃ for overnight drying.
4. The dried white powder was thoroughly ground and calcined in an air atmosphere at 600 ℃ for 10 h.
5. And (3) putting 0.5g of calcined white powder and 20g of urea into an agate mortar, fully mixing, transferring into a ceramic crucible, sealing by using 4 layers of tinfoil paper, putting into a muffle furnace, heating to 550 ℃ at the speed of 4 ℃/min, and calcining for 2 hours at the temperature to obtain a yellow honeycomb solid.
6. And (3) fully grinding the yellow solid, filtering and washing the ground yellow solid by using deionized water, and then placing the washed yellow solid in a vacuum oven at 80 ℃ for overnight drying to obtain the PCN doped with potassium ions in a gradient manner, wherein the PCN is marked as (K) PCN & KTO (600) -2.5-2 h.
7. Weighing 50mg (K) PCN&Ultrasonically dispersing a KTO (600) -2.5-2H sample in 80mL of pure water, adding 20mL of methanol serving as a sacrificial agent, and adding 37mL of chloroplatinic acid (H)2PtCl6) The aqueous solution (1.48mgPt/mL) is placed in a Pyrex materialIn the glass photocatalytic reactor, a 300W xenon lamp is used as a light source, a Pt-loaded cocatalyst is irradiated for 2h in-situ light deposition under a visible light wave band (not less than 420nm), and then hydrogen production activity test is carried out every hour. The hydrogen generated by the photocatalytic reaction is quantitatively sampled and analyzed by a gas chromatograph with a thermal conductivity detector, and the average hydrogen production rate is 12.8 mu mol/h.
Comparative example 1
The comparative example relates to the effect of different potassium ion sources on the gradient doping effect, and the preparation method of the comparative example is only different from that of example 1 in that KTaO of perovskite type is replaced3(abbreviated as KTOper) The particles were doped with PCN and the sample was reported as (K) PCN&KTOper. The main synthesis steps are as follows:
1. 96g of potassium hydroxide solid is dissolved in 100mL of pure water and fully stirred to obtain a potassium hydroxide solution, 5g of tantalum (V) oxide is added, and then ultrasonic treatment is carried out for 10min and stirring is carried out to obtain a uniform white suspension.
2. The solution was transferred to a 100mL Teflon liner and heated in a 200 ℃ oven for 8h in a hydrothermal kettle. The alkalization hydrothermal time, reaction temperature and pH affect the product crystal form. Increasing the hydrothermal time and increasing the hydrothermal temperature increases the concentration of KOH and results in a perovskite-type product. In this comparative example, the hydrothermal temperature was 200 deg.C
3. Separating the white solid powder after the hydrothermal alkalization reaction from the supernatant alkali liquor, centrifugally washing the white solid powder for 5 times until the pH value of the centrifugate is 7, and then placing the centrifugally treated solid in a vacuum oven at 80 ℃ for overnight drying.
4. The dried white powder was thoroughly ground and calcined in an air atmosphere at 600 ℃ for 10 h.
5. And (3) putting 0.5g of calcined white powder and 20g of urea into an agate mortar for full mixing, transferring the mixture into a ceramic crucible, sealing the mixture by using 4 layers of tinfoil paper, putting the mixture into a muffle furnace, heating the mixture to 550 ℃ at the speed of 2.5 ℃/min, and calcining the mixture for 4 hours at the temperature to obtain a yellow honeycomb-shaped solid.
6. Grinding the yellow solid sufficiently, filtering and washing the ground yellow solid by deionized water, and then placing the ground yellow solid in a vacuum oven at 80 ℃ for overnight drying to obtain potassium ionsGradient doped PCN, denoted (K) PCN&KTOper-2.5%-4h。
7. Weighing 50mg (K) PCN&KTOperUltrasonically dispersing a sample in 80mL of pure water for 2.5-4H, adding 20mL of methanol serving as a sacrificial agent, and adding 37mL of chloroplatinic acid (H)2PtCl6) The aqueous solution (1.48mgPt/mL) is placed in a Pyrex glass photocatalytic reactor, a 300W xenon lamp is used as a light source, the Pt promoter is loaded by irradiating for 2h of in-situ light deposition under a visible light wave band (not less than 420nm), and then the hydrogen production activity test is carried out every hour. The hydrogen produced by the photocatalytic reaction is quantitatively sampled and analyzed by a gas chromatograph with a thermal conductivity detector, and the average hydrogen production rate is 3.6 mu mol/h.
As shown in fig. 3, KTO was prepared by hydrothermal alkalizationperThe cubic structure of typical perovskite crystal form is presented.
KTO as shown in FIG. 4perGood composite contact is formed between the particles and the layered PCN.
As shown in FIG. 8, with KTOper(K) PCN with particles doped as a source of potassium ions&KTOperThe sample did not exhibit effective potassium doping. Elemental distribution display of high resolution TEM as KTOperThe particles are taken as a source, no obvious K element is distributed, the K/N atomic ratio is close to zero along Line # 1 and Line # 2, and the conditions that the diffusion doping of the potassium ions does not occur and the KTO is generated are shownperThe particles are not suitable as a diffusion source for potassium ions.
By KTOper(K) PCN with particles doped as a source of potassium ions&KTOperThe hydrogen production activity of the sample is 3.6 mu mol/h, which is lower than that of KTOpyrThe PCN sample doped with particles as a potassium ion source was close in activity to the unmodified blank PCN.
Comparative example 2
The comparative example relates to the effect of different potassium ion sources on the gradient doping effect, and the preparation method is different from the example 1 only in that PCN doping is performed by replacing conventional KOH particles, and the sample is marked as (K) PCN & KOH.
1. Potassium hydroxide granules (potassium content equivalent to example 1) and 20g of urea were taken, placed in an agate mortar and thoroughly mixed, transferred into a ceramic crucible, sealed with 4 layers of tinfoil, placed in a muffle furnace, heated to 550 ℃ at a rate of 2.5 ℃/min, and calcined at the temperature for 4h to obtain a yellow honeycomb solid.
2. And fully grinding the yellow solid, filtering and washing the ground yellow solid by using deionized water, and then placing the washed yellow solid in a vacuum oven at 80 ℃ for overnight drying to obtain the PCN doped with potassium ions, wherein the mark is (K) PCN & KOH.
3. Weighing 50mg (K) PCN&The KOH sample was ultrasonically dispersed in 80mL of pure water, 20mL of methanol was added as a sacrificial agent, and 37mL of chloroplatinic acid (H) was added2PtCl6) The aqueous solution (1.48mgPt/mL) is placed in a Pyrex glass photocatalytic reactor, a 300W xenon lamp is used as a light source, the Pt promoter is firstly irradiated for 2h in-situ light deposition loading under a visible light wave band (more than or equal to 420nm), and then hydrogen production activity test is carried out every hour. The hydrogen produced by the photocatalytic reaction is quantitatively sampled and analyzed by a gas chromatograph with a thermal conductivity detector, and the average hydrogen production rate is 8.6 mu mol/h.
As shown in fig. 5, the modified PCN doped with KOH as a potassium source still retained a stable layered structure.
As shown in fig. 9, the (K) PCN & KOH samples doped with KOH as a potassium ion source exhibited uniform potassium doping. The element distribution of the high-resolution TEM shows that KOH particles are used as a source, K elements are uniformly distributed, and the K/N atomic ratio is kept between 3% and 5% along Line # 1 and Line # 2, which indicates that the doping of potassium ions occurs and the gradient diffusion distribution is not formed.
(K) PCN doped with KOH as a source of potassium ions&The hydrogen production activity of the KOH sample is 8.6 mu mol/h which is lower than that of KTOpyr(K) PCN with particles doped as a source of potassium ions&KTO sample, which shows that gradient doping modification of potassium ions is superior to uniform doping modification.
Comparative example 3
The comparative example relates to the influence of different potassium ion sources on the gradient doping effect, and the preparation method of the carbon nitride material is different from that of the carbon nitride material in example 1 only in that no potassium tantalate particles are added to prepare a blank non-modified carbon nitride material, and the sample is marked as PCN.
1. 20g of urea is placed in an agate mortar and is fully mixed, then the mixture is transferred into a ceramic crucible and is sealed by 4 layers of tin foil paper, the mixture is placed in a muffle furnace, the temperature is raised to 550 ℃ at the speed of 2.5 ℃/min, and the mixture is calcined for 4 hours at the temperature to obtain yellow honeycomb solid.
2. And fully grinding the yellow solid, filtering and washing the ground yellow solid by using deionized water, and then placing the washed yellow solid in a vacuum oven at 80 ℃ for overnight drying to obtain blank non-modified PCN.
3. A50 mg sample of PCN was weighed, ultrasonically dispersed in 80mL of pure water, 20mL of methanol was added as a sacrificial agent, and 37mL of chloroplatinic acid (H) was added2PtCl6) The aqueous solution (1.48mgPt/mL) is placed in a Pyrex glass photocatalytic reactor, a 300W xenon lamp is used as a light source, the Pt promoter is firstly irradiated for 2h in-situ light deposition loading under a visible light wave band (more than or equal to 420nm), and then hydrogen production activity test is carried out every hour. The hydrogen generated by the photocatalytic reaction is quantitatively sampled and analyzed by a gas chromatograph with a thermal conductivity detector, and the average hydrogen production rate is 3.1 mu mol/h.
As shown in fig. 6, the PCN material synthesized by the calcination polymerization method exhibits a layered stack.
The foregoing description of specific embodiments of the present invention has been presented. It is to be understood that the present invention is not limited to the specific embodiments described above, and that various changes and modifications may be made by one skilled in the art within the scope of the appended claims without departing from the spirit of the invention.
Claims (10)
1. The preparation method of the potassium ion gradient doped carbon nitride material is characterized by comprising the following steps of:
s1, mixing tantalum oxide powder with a potassium hydroxide solution to obtain a white suspension, heating for reaction, and centrifuging to obtain a white solid;
s2, calcining and crystallizing the white solid to obtain pyrochlore type potassium tantalate solid powder serving as a potassium ion source;
s3, mixing the potassium ion source potassium tantalate solid powder with the carbon nitride precursor, sealing and heating to obtain the potassium ion gradient doped carbon nitride material.
2. The method according to claim 1, wherein the concentration of the potassium hydroxide solution in step S1 is 6mol/L to 12 mol/L.
3. The method according to claim 1, wherein the ratio of the amount of the potassium hydroxide solution to the amount of the tantalum oxide is 100 mL: 5-8 g.
4. The method according to claim 1, wherein the heating reaction in step S1 is carried out at a temperature of 120 ℃ to 180 ℃ for a time of 6h to 12 h.
5. The preparation method of claim 1, wherein the temperature of the calcination crystallization in the step S2 is 400-800 ℃, and the time of the calcination crystallization is 6-12 h.
6. The method according to claim 1, wherein the solid powder of potassium tantalate as the potassium ion source used in step S3 is 0.5 to 10% by mass based on the mass of the carbon nitride precursor.
7. The method of claim 1, wherein the carbon nitride precursor comprises one of urea and melamine.
8. The method according to claim 1, wherein the heating in step S3 is performed at a temperature of 500 ℃ to 600 ℃ for a time of 3h to 6 h.
9. The method of claim 1, wherein the heated product is fully ground in step S3, washed with water, dried, and ground to obtain the potassium ion gradient doped carbon nitride material.
10. Application of the potassium ion gradient doped carbon nitride material as defined in claim 1 in the field of hydrogen production through photocatalytic water decomposition.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202210422019.XA CN114768852B (en) | 2022-04-21 | 2022-04-21 | Preparation method of potassium ion gradient doped carbon nitride material |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202210422019.XA CN114768852B (en) | 2022-04-21 | 2022-04-21 | Preparation method of potassium ion gradient doped carbon nitride material |
Publications (2)
Publication Number | Publication Date |
---|---|
CN114768852A true CN114768852A (en) | 2022-07-22 |
CN114768852B CN114768852B (en) | 2023-05-26 |
Family
ID=82432108
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN202210422019.XA Active CN114768852B (en) | 2022-04-21 | 2022-04-21 | Preparation method of potassium ion gradient doped carbon nitride material |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN114768852B (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN115845902A (en) * | 2022-12-08 | 2023-03-28 | 上海交通大学深圳研究院 | Graphite phase carbon nitride photocatalytic material and preparation method thereof |
Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105879871A (en) * | 2016-05-03 | 2016-08-24 | 上海交通大学 | Method for preparing plasma gold nanorod composite photocatalytic material with butterfly wing structure |
CN106732728A (en) * | 2016-12-27 | 2017-05-31 | 常州大学 | It is a kind of effectively to reduce carbonitride (g C3N4) the green wood preparation method for material of TOC is contributed in nanometer sheet photocatalytic process |
CN108187718A (en) * | 2017-12-28 | 2018-06-22 | 江苏大学 | A kind of Preparation method and use of carbonitride/tantalic acid calcium potassium nanosheet composite material |
CN109569681A (en) * | 2017-09-28 | 2019-04-05 | 湖南大学 | Silver nanoparticles loaded and the sodium tantalate composite photo-catalyst of graphite phase carbon nitride nanometer sheet and its preparation method and application |
CN110116988A (en) * | 2018-02-07 | 2019-08-13 | 中国科学院武汉物理与数学研究所 | A kind of preparation method of photodissociation aquatic products hydrogen |
JP2020157283A (en) * | 2019-03-28 | 2020-10-01 | 公立大学法人山陽小野田市立山口東京理科大学 | Method for producing photocatalyst |
CN112675889A (en) * | 2020-12-11 | 2021-04-20 | 福建江夏学院 | Synthesis method of potassium-sodium niobate-carbon nitride photocatalytic composite material and product thereof |
CN113694956A (en) * | 2021-09-23 | 2021-11-26 | 辽宁大学 | Nitrogen-doped potassium tantalate photocatalyst and preparation method and application thereof |
-
2022
- 2022-04-21 CN CN202210422019.XA patent/CN114768852B/en active Active
Patent Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105879871A (en) * | 2016-05-03 | 2016-08-24 | 上海交通大学 | Method for preparing plasma gold nanorod composite photocatalytic material with butterfly wing structure |
CN106732728A (en) * | 2016-12-27 | 2017-05-31 | 常州大学 | It is a kind of effectively to reduce carbonitride (g C3N4) the green wood preparation method for material of TOC is contributed in nanometer sheet photocatalytic process |
CN109569681A (en) * | 2017-09-28 | 2019-04-05 | 湖南大学 | Silver nanoparticles loaded and the sodium tantalate composite photo-catalyst of graphite phase carbon nitride nanometer sheet and its preparation method and application |
CN108187718A (en) * | 2017-12-28 | 2018-06-22 | 江苏大学 | A kind of Preparation method and use of carbonitride/tantalic acid calcium potassium nanosheet composite material |
CN110116988A (en) * | 2018-02-07 | 2019-08-13 | 中国科学院武汉物理与数学研究所 | A kind of preparation method of photodissociation aquatic products hydrogen |
JP2020157283A (en) * | 2019-03-28 | 2020-10-01 | 公立大学法人山陽小野田市立山口東京理科大学 | Method for producing photocatalyst |
CN112675889A (en) * | 2020-12-11 | 2021-04-20 | 福建江夏学院 | Synthesis method of potassium-sodium niobate-carbon nitride photocatalytic composite material and product thereof |
CN113694956A (en) * | 2021-09-23 | 2021-11-26 | 辽宁大学 | Nitrogen-doped potassium tantalate photocatalyst and preparation method and application thereof |
Non-Patent Citations (3)
Title |
---|
余竞雄: "铌酸钾体系光催化剂的制备及其光催化性能研究", 《中国优秀硕士学位论文全文数据库 工程科技Ⅰ辑》 * |
北京师范大学等编: "《无机化学(上下册)》", 28 February 1982 * |
廖金龙等: "g-C_3N_4/NaTaO_3复合材料的制备及可见光催化性能", 《浙江理工大学学报(自然科学版)》 * |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN115845902A (en) * | 2022-12-08 | 2023-03-28 | 上海交通大学深圳研究院 | Graphite phase carbon nitride photocatalytic material and preparation method thereof |
CN115845902B (en) * | 2022-12-08 | 2024-04-19 | 上海交通大学深圳研究院 | Graphite-phase carbon nitride photocatalytic material and preparation method thereof |
Also Published As
Publication number | Publication date |
---|---|
CN114768852B (en) | 2023-05-26 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
Wang et al. | Fabrication of Bi4Ti3O12/ZnIn2S4 S-scheme heterojunction for achieving efficient photocatalytic hydrogen production | |
CN110124706B (en) | Preparation method of titanium carbide/indium zinc sulfide composite visible-light-driven photocatalyst | |
CN107876087B (en) | preparation of methylamine lead iodine-reduced graphene oxide composite photocatalytic material and application of composite photocatalytic material in photocatalytic hydrogen production | |
Hu et al. | LaMnO3 nanoparticles supported on N doped porous carbon as efficient photocatalyst | |
CN112023938B (en) | Bimetallic ion doped nano composite photocatalyst and preparation method thereof | |
Xue et al. | C3N4 nanosheets loaded with the CuWO4 activated NiS co-catalyst: a stable noble metal-free photocatalyst with dramatic photocatalytic activity for H2 generation and high salinity tolerant | |
Choi et al. | Enhanced photoelectrochemical efficiency and stability using nitrogen-doped TiO2 on a GaAs photoanode | |
CN111604063A (en) | g-C3N4/In2Se3Composite photocatalyst and preparation method and application thereof | |
CN114768852B (en) | Preparation method of potassium ion gradient doped carbon nitride material | |
CN109046391B (en) | Composite material, preparation method thereof and application thereof in hydrogen production through visible light decomposition of water | |
Gong et al. | Enhanced photocatalytic hydrogen production performance of g-C3N4 with rich carbon vacancies | |
CN108054396B (en) | Nitrogen-doped graphene/cobaltous oxide composite material and preparation method thereof | |
Song et al. | Bi 3 TaO 7 film: a promising photoelectrode for photoelectrochemical water splitting | |
CN115110115B (en) | C, N co-doped TiO 2-based composite film photoelectrode and preparation method and application thereof | |
CN108821394B (en) | Preparation method of iron (II) molybdate/graphene oxide catalytic electrode | |
Dang et al. | An integrated approach to construct tantalum derivatives for electrocatalysis beyond the triiodide reduction reaction | |
Liu et al. | Enhanced photocatalytic degradation performance of mono-disperse ZnS nano-flake on biocarbon sheets | |
CN105088266A (en) | Method for compounding co-catalyst on semiconductor material to manufacture photoelectric chemical cell nano-structure photoelectrode | |
CN115090318A (en) | Preparation method and application of intermolecular heterojunction carbon nitride photocatalyst with high specific surface area | |
CN109078636B (en) | Plasma photocatalyst, preparation method thereof and application thereof in hydrogen production | |
CN114192163A (en) | SrTiO doped with K ions of externally tangent 36-plane {110} crystal face3Nano photocatalyst and preparation method thereof | |
CN113797940A (en) | Cobalt selenide graphite carbon nitride composite material and preparation method and application thereof | |
Jiang et al. | Utilizing stress release effect for achieving high-performance photoelectrochemical hydrogen evolution on CQDs-enriched SnSe nanosheets | |
Qiao et al. | Visible light responsive photocatalytic fuel cell with Ce-UiO-66/g-C3N4/Bi2WO6/Ti photoanode for simultaneous degradation of rhodamine B and electricity generation | |
CN114797849B (en) | Bifunctional perovskite oxide catalyst, preparation method and application 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 |