CN113479896B - Method for preparing calcium copper silicate material by using attapulgite and biomass and application of calcium copper silicate material - Google Patents
Method for preparing calcium copper silicate material by using attapulgite and biomass and application of calcium copper silicate material Download PDFInfo
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- CN113479896B CN113479896B CN202110805500.2A CN202110805500A CN113479896B CN 113479896 B CN113479896 B CN 113479896B CN 202110805500 A CN202110805500 A CN 202110805500A CN 113479896 B CN113479896 B CN 113479896B
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- 239000000463 material Substances 0.000 title claims abstract description 40
- 229960000892 attapulgite Drugs 0.000 title claims abstract description 32
- 229910052625 palygorskite Inorganic materials 0.000 title claims abstract description 32
- VAELQCZFRATZQB-UHFFFAOYSA-N calcium copper silicate Chemical compound [Ca+2].[Cu+2].[O-][Si]([O-])([O-])[O-] VAELQCZFRATZQB-UHFFFAOYSA-N 0.000 title claims abstract description 26
- 239000002028 Biomass Substances 0.000 title claims abstract description 25
- 238000000034 method Methods 0.000 title claims abstract description 23
- 239000000843 powder Substances 0.000 claims abstract description 42
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims abstract description 34
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 claims abstract description 28
- 238000001035 drying Methods 0.000 claims abstract description 17
- 238000002156 mixing Methods 0.000 claims abstract description 15
- 230000001699 photocatalysis Effects 0.000 claims abstract description 15
- 229910021529 ammonia Inorganic materials 0.000 claims abstract description 14
- 238000001354 calcination Methods 0.000 claims abstract description 12
- BFNBIHQBYMNNAN-UHFFFAOYSA-N ammonium sulfate Chemical compound N.N.OS(O)(=O)=O BFNBIHQBYMNNAN-UHFFFAOYSA-N 0.000 claims abstract description 10
- 229910052921 ammonium sulfate Inorganic materials 0.000 claims abstract description 10
- 235000011130 ammonium sulphate Nutrition 0.000 claims abstract description 10
- 239000007787 solid Substances 0.000 claims abstract description 10
- 238000003786 synthesis reaction Methods 0.000 claims abstract description 10
- 230000015572 biosynthetic process Effects 0.000 claims abstract description 9
- 238000002360 preparation method Methods 0.000 claims abstract description 6
- 159000000007 calcium salts Chemical class 0.000 claims abstract description 4
- 238000001816 cooling Methods 0.000 claims description 18
- 239000000203 mixture Substances 0.000 claims description 15
- 239000010949 copper Substances 0.000 claims description 13
- 239000007788 liquid Substances 0.000 claims description 10
- 102000002322 Egg Proteins Human genes 0.000 claims description 9
- 108010000912 Egg Proteins Proteins 0.000 claims description 9
- 239000000919 ceramic Substances 0.000 claims description 9
- 210000003278 egg shell Anatomy 0.000 claims description 9
- 238000000227 grinding Methods 0.000 claims description 9
- 238000010438 heat treatment Methods 0.000 claims description 9
- 238000005406 washing Methods 0.000 claims description 9
- 238000003756 stirring Methods 0.000 claims description 8
- 229910004298 SiO 2 Inorganic materials 0.000 claims description 7
- 229910052802 copper Inorganic materials 0.000 claims description 7
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims description 6
- 239000002253 acid Substances 0.000 claims description 5
- 239000000378 calcium silicate Substances 0.000 claims description 5
- 229910052918 calcium silicate Inorganic materials 0.000 claims description 5
- OYACROKNLOSFPA-UHFFFAOYSA-N calcium;dioxido(oxo)silane Chemical compound [Ca+2].[O-][Si]([O-])=O OYACROKNLOSFPA-UHFFFAOYSA-N 0.000 claims description 5
- 239000008367 deionised water Substances 0.000 claims description 5
- 229910021641 deionized water Inorganic materials 0.000 claims description 5
- 238000007146 photocatalysis Methods 0.000 claims description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 5
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims description 4
- 150000003863 ammonium salts Chemical class 0.000 claims description 4
- PAWQVTBBRAZDMG-UHFFFAOYSA-N 2-(3-bromo-2-fluorophenyl)acetic acid Chemical compound OC(=O)CC1=CC=CC(Br)=C1F PAWQVTBBRAZDMG-UHFFFAOYSA-N 0.000 claims description 2
- ATRRKUHOCOJYRX-UHFFFAOYSA-N Ammonium bicarbonate Chemical compound [NH4+].OC([O-])=O ATRRKUHOCOJYRX-UHFFFAOYSA-N 0.000 claims description 2
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 claims description 2
- 239000001099 ammonium carbonate Substances 0.000 claims description 2
- 235000012501 ammonium carbonate Nutrition 0.000 claims description 2
- ZMMDPCMYTCRWFF-UHFFFAOYSA-J dicopper;carbonate;dihydroxide Chemical compound [OH-].[OH-].[Cu+2].[Cu+2].[O-]C([O-])=O ZMMDPCMYTCRWFF-UHFFFAOYSA-J 0.000 claims description 2
- 238000005286 illumination Methods 0.000 claims description 2
- 238000003760 magnetic stirring Methods 0.000 claims description 2
- 238000010907 mechanical stirring Methods 0.000 claims description 2
- 229910017604 nitric acid Inorganic materials 0.000 claims description 2
- 238000013032 photocatalytic reaction Methods 0.000 claims description 2
- 230000000630 rising effect Effects 0.000 claims 1
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 abstract description 20
- 239000000047 product Substances 0.000 abstract description 11
- 229910052757 nitrogen Inorganic materials 0.000 abstract description 10
- 239000003054 catalyst Substances 0.000 abstract description 5
- 230000000694 effects Effects 0.000 abstract description 5
- 229910052500 inorganic mineral Inorganic materials 0.000 abstract description 5
- 239000011707 mineral Substances 0.000 abstract description 5
- 239000002994 raw material Substances 0.000 abstract description 5
- 229940116318 copper carbonate Drugs 0.000 abstract 1
- GEZOTWYUIKXWOA-UHFFFAOYSA-L copper;carbonate Chemical compound [Cu+2].[O-]C([O-])=O GEZOTWYUIKXWOA-UHFFFAOYSA-L 0.000 abstract 1
- 239000002244 precipitate Substances 0.000 abstract 1
- 238000004519 manufacturing process Methods 0.000 description 9
- 238000006243 chemical reaction Methods 0.000 description 6
- 238000001514 detection method Methods 0.000 description 6
- 229910052791 calcium Inorganic materials 0.000 description 5
- 239000011575 calcium Substances 0.000 description 5
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 4
- 239000011941 photocatalyst Substances 0.000 description 4
- BHPQYMZQTOCNFJ-UHFFFAOYSA-N Calcium cation Chemical compound [Ca+2] BHPQYMZQTOCNFJ-UHFFFAOYSA-N 0.000 description 3
- BPQQTUXANYXVAA-UHFFFAOYSA-N Orthosilicate Chemical compound [O-][Si]([O-])([O-])[O-] BPQQTUXANYXVAA-UHFFFAOYSA-N 0.000 description 3
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical group [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- MKYBYDHXWVHEJW-UHFFFAOYSA-N N-[1-oxo-1-(2,4,6,7-tetrahydrotriazolo[4,5-c]pyridin-5-yl)propan-2-yl]-2-[[3-(trifluoromethoxy)phenyl]methylamino]pyrimidine-5-carboxamide Chemical compound O=C(C(C)NC(=O)C=1C=NC(=NC=1)NCC1=CC(=CC=C1)OC(F)(F)F)N1CC2=C(CC1)NN=N2 MKYBYDHXWVHEJW-UHFFFAOYSA-N 0.000 description 2
- 238000002441 X-ray diffraction Methods 0.000 description 2
- 230000004913 activation Effects 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 229910001424 calcium ion Inorganic materials 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 230000007547 defect Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 235000010755 mineral Nutrition 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 230000004044 response Effects 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- 230000002194 synthesizing effect Effects 0.000 description 2
- 229910018072 Al 2 O 3 Inorganic materials 0.000 description 1
- 229910004762 CaSiO Inorganic materials 0.000 description 1
- JPVYNHNXODAKFH-UHFFFAOYSA-N Cu2+ Chemical compound [Cu+2] JPVYNHNXODAKFH-UHFFFAOYSA-N 0.000 description 1
- 238000009620 Haber process Methods 0.000 description 1
- 241000907663 Siproeta stelenes Species 0.000 description 1
- 238000003917 TEM image Methods 0.000 description 1
- 229910010413 TiO 2 Inorganic materials 0.000 description 1
- 238000002835 absorbance Methods 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 229910000019 calcium carbonate Inorganic materials 0.000 description 1
- 239000000969 carrier Substances 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 150000001768 cations Chemical class 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 239000004927 clay Substances 0.000 description 1
- 229910001431 copper ion Inorganic materials 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 229910021645 metal ion Inorganic materials 0.000 description 1
- 238000001465 metallisation Methods 0.000 description 1
- 230000005012 migration Effects 0.000 description 1
- 238000013508 migration Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 229910000510 noble metal Inorganic materials 0.000 description 1
- 238000000643 oven drying Methods 0.000 description 1
- 239000012071 phase Substances 0.000 description 1
- 230000010287 polarization Effects 0.000 description 1
- 238000000634 powder X-ray diffraction Methods 0.000 description 1
- 238000003746 solid phase reaction Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 239000006228 supernatant Substances 0.000 description 1
- 229910052723 transition metal Inorganic materials 0.000 description 1
- 150000003624 transition metals Chemical class 0.000 description 1
- 238000005303 weighing Methods 0.000 description 1
- 229910052724 xenon Inorganic materials 0.000 description 1
- FHNFHKCVQCLJFQ-UHFFFAOYSA-N xenon atom Chemical compound [Xe] FHNFHKCVQCLJFQ-UHFFFAOYSA-N 0.000 description 1
Classifications
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B33/00—Silicon; Compounds thereof
- C01B33/20—Silicates
-
- 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
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/002—Mixed oxides other than spinels, e.g. perovskite
-
- 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
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
- B01J23/72—Copper
-
- B01J35/39—
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01C—AMMONIA; CYANOGEN; COMPOUNDS THEREOF
- C01C1/00—Ammonia; Compounds thereof
- C01C1/02—Preparation, purification or separation of ammonia
- C01C1/04—Preparation of ammonia by synthesis in the gas phase
- C01C1/0405—Preparation of ammonia by synthesis in the gas phase from N2 and H2 in presence of a catalyst
- C01C1/0411—Preparation of ammonia by synthesis in the gas phase from N2 and H2 in presence of a catalyst characterised by the catalyst
-
- 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
- B01J2523/00—Constitutive chemical elements of heterogeneous catalysts
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2002/00—Crystal-structural characteristics
- C01P2002/70—Crystal-structural characteristics defined by measured X-ray, neutron or electron diffraction data
- C01P2002/72—Crystal-structural characteristics defined by measured X-ray, neutron or electron diffraction data by d-values or two theta-values, e.g. as X-ray diagram
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2004/00—Particle morphology
- C01P2004/01—Particle morphology depicted by an image
- C01P2004/04—Particle morphology depicted by an image obtained by TEM, STEM, STM or AFM
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2004/00—Particle morphology
- C01P2004/20—Particle morphology extending in two dimensions, e.g. plate-like
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2004/00—Particle morphology
- C01P2004/50—Agglomerated particles
-
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/52—Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts
Abstract
The application belongs to the technical field of novel material preparation and photocatalytic ammonia synthesis, and in particular relates to a method for preparing a calcium copper silicate material by utilizing attapulgite and biomass and application thereof, wherein attapulgite powder and ammonium sulfate are mixed and calcined, the obtained calcined product is uniformly dispersed into hydrochloric acid solution with a certain concentration, solid precipitate is washed, and SiO is obtained by drying 2 And (3) powder. SiO produced 2 Mixing and calcining the powder, the biomass containing calcium salt and basic copper carbonate to obtain a calcium copper silicate material, and applying the calcium copper silicate material to photocatalytic nitrogen fixation synthesis of ammonia. The method is characterized in that mineral attapulgite rich in nature is skillfully utilized as a raw material, the structure of the mineral attapulgite is recombined, and the calcium copper silicate catalyst with good nitrogen fixation effect is prepared by combining the mineral attapulgite with the rest of cheap biomass materials.
Description
Technical Field
The application belongs to the technical field of novel material preparation and photocatalytic ammonia synthesis, and particularly relates to a method for preparing a calcium copper silicate material by using attapulgite and biomass and application thereof.
Background
The Haber-Bosch process using an iron-based catalyst has been widely used for industrial synthesis of ammonia, but the reaction needs to be performed at high temperature and high pressure, and the energy consumption is huge, and a new process for synthesizing ammonia is needed to be found in the present day of the increasing shortage of energy. In recent years, photocatalytic ammonia synthesis reaction has been widely focused, and the principle is to utilize sunlight to realize conversion from nitrogen to ammonia under the action of a catalyst. However, at present, noble metal deposition or ion doping and other methods are mostly adopted to improve the nitrogen fixation effect of the photocatalyst, so that the cost is high. In addition, part of the catalyst is such as TiO 2 And the photocatalytic performance of the light-emitting diode is seriously affected due to the fact that the light utilization rate of the light-emitting diode is not high due to the high bandwidth.
Disclosure of Invention
The application aims to overcome the problems in the prior art, and provides a preparation and application of a photocatalysis synthesis ammonia catalyst with low cost, easily available raw materials and high photo-generated electron hole separation efficiency, in particular to a method for preparing a calcium copper silicate material by using attapulgite and biomass and application thereof. The preparation method is simple, the synthesis condition is mild, complex and expensive equipment is not needed, and the method is favorable for large-scale popularization.
In order to achieve the purpose of the application, the technical scheme adopted is as follows:
a method for preparing a calcium copper silicate material by using attapulgite and biomass comprises the following steps:
(1) Mixing attapulgite powder and ammonium salt at a mass ratio of 1:1 to the upper partMixing at a ratio of 1:5, placing the mixture in a ceramic crucible, placing the crucible in a muffle furnace, and raising the temperature to 400-700 ℃ at a speed of 1-8 ℃/min (SiO obtained beyond the range) 2 With more impurities, e.g. MgO, caO or Al 2 O 3 And the like, preferably heating to 500 ℃ at 2 ℃ per minute), then naturally cooling to room temperature, dispersing the obtained calcined product into an acid solution, hydrothermally stirring for 1-5 hours, separating out solids (preferably, hydrochloric acid concentration is 2mol/L, solid-to-liquid ratio of the calcined product to the hydrochloric acid is 1:20, and the temperature of the hydrothermally stirring is 80 ℃), washing and drying to obtain white SiO 2 And (3) powder.
(2) Mixing basic cupric carbonate and calcium salt-containing biomass (preferably, eggshell powder and/or shell powder, and in response to selection of biomass mainly containing calcium element) with SiO obtained in step (1) 2 The molar ratio of the powder is 0.5-1: 0.5 to 1: calcining for 1-5 h at 800-1000 ℃ after mixing the materials with a feeding ratio of 0.5-5 (calcium copper silicate material can not be obtained after less than 1h, and the calcium copper silicate is in a lump shape and is not a two-dimensional sheet layer after more than 5h, preferably 2 h), naturally cooling to room temperature, grinding and drying to obtain the calcium copper silicate material.
Further, the obtained calcined product is dispersed into hydrochloric acid solution in the step (1) and is stirred for 1 to 5 hours in a hydrothermal mode, wherein the hydrothermal stirring method is mechanical stirring or magnetic stirring.
Further, in the step (1), the ammonium salt is ammonium sulfate, ammonium nitrate or basic ammonium carbonate.
Further, the acid solution in the step (1) is hydrochloric acid, sulfuric acid or nitric acid solution.
The calcium silicate copper material prepared by the method is applied to photocatalytic synthesis of ammonia.
The specific application method is as follows: dispersing the calcium silicate copper material in deionized water, then adding the deionized water into a photocatalytic reaction device, and introducing N 2 And carrying out photocatalysis by illumination to obtain ammonia.
In the application, the attapulgite is used as a natural mineral clay material, has rich reserves in China, and has large specific surface area and unique one-dimensional nano rod-shaped structure due to good dispersibility. Because the attapulgite is rich in SiO 2 SiO can be produced by completely destroying its octahedral structure 2 Raw materials and ensure that the rod-shaped structure is unchanged, and SiO in transition metal cation silicate 4 Tetrahedra are susceptible to twisting and polarization, thereby enhancing migration of the photo-active carriers. In addition, silicate-based photocatalysts have broad prospects due to their low cost and abundant reserves. In addition, the main component of the calcium-containing biomass material such as eggshell powder, shell powder and the like is calcium carbonate, calcium ions and copper ions are introduced into the catalytic material through calcination, the calcium-containing biomass material has better adsorption and activation effects on nitrogen in the nitrogen fixation process, the faster reaction proceeding speed is determined, and the introduced calcium and copper metal ions can manufacture defect sites in the material, so that the adsorption and activation of the nitrogen are realized. In addition, the introduction of calcium ions can also cause lattice distortion in the original silicate structure to generate oxygen vacancies, and the oxygen vacancies and defect sites can cooperatively adsorb and activate nitrogen molecules, so that the efficiency of photocatalytic nitrogen fixation is improved.
Therefore, compared with the prior art, the application has the advantages that: the method is characterized in that minerals such as natural attapulgite, malachite and the like rich in nature and calcium-containing biomass are selected as raw materials, metal elements Ca and Cu are introduced, and a novel calcium-copper silicate photocatalyst which has a stable structure, a two-dimensional lamellar structure, high photoproduction electron-hole separation efficiency and good photocatalytic ammonia synthesis effect is synthesized by means of high-temperature solid phase reaction; meanwhile, the method has the advantages of rich raw material sources, low cost, environmental friendliness, simple and convenient preparation process and contribution to large-scale popularization.
Drawings
FIG. 1 is a diagram of 800-CaCuSi prepared in example 1 4 O 10 An XRD pattern of (a) and a corresponding PDF card;
FIG. 2 is a diagram of 800-CaCuSi prepared in example 1 4 O 10 TEM image of the 100nm scale range of the sample.
Detailed Description
The present application is not limited to the following embodiments, and those skilled in the art can implement the present application in various other embodiments according to the present application, or simply change or modify the design structure and thought of the present application, which fall within the protection scope of the present application. It should be noted that, without conflict, the embodiments of the present application and features of the embodiments may be combined with each other.
The application is further described in detail below in connection with the examples:
example 1
(1) 5g of attapulgite powder and ammonium sulfate are mixed according to the mass ratio of 1:1, mixing and placing the mixture into a ceramic crucible, placing the crucible into a muffle furnace, heating to 500 ℃ at a speed of 2 ℃/min, then naturally cooling to room temperature, and obtaining a calcined product according to a solid-to-liquid ratio of 1:20 are dispersed into 2mol/L hydrochloric acid solution, solid is separated out after being stirred for 6 hours under 80 ℃ in a hydrothermal mode, and white SiO is obtained after washing and drying 2 And (3) powder.
(2) 1.11g Cu 2 (OH) 2 CO 3 And 0.6g of prepared SiO from 1.0g of eggshell powder 2 Placing the powder and the mixture in a crucible, transferring to a muffle furnace, calcining for 2h at 800 ℃, naturally cooling to room temperature, grinding and drying to obtain a calcium silicate copper material, namely 800-CaCuSi 4 O 10 。
For 800-CaCuSi prepared in this example 4 O 10 The material is subjected to X-ray powder diffraction to analyze the phase, and the appearance and the structure of the material are observed under a transmission electron microscope.
XRD patterns are shown in FIG. 1, by comparison with CaCuSi 4 O 10 The PDF card of (2) shows CaCuSi at 11.6 °, 23.2 °, 26.3 °, 39.6 °, etc 4 O 10 Characteristic diffraction characteristic peaks, and no impurity peaks, indicate that the 800-CaCuSi prepared by the method 4 O 10 Relatively pure, combined with TEM photograph FIG. 2, can prove 800-CaCuSi 4 O 10 Is a multi-layer stack of two-dimensional sheets.
The application also provides an application method of the photocatalyst for synthesizing ammonia by photocatalysis.
The application method comprises the following steps: weighing the prepared calcium copper silicate material 800-CaCuSi 4 O 10 0.04g was dissolved in 100mL deionized water,then adding the mixture into a photocatalysis reaction device, N 2 Introducing into a reaction device at a flow rate of 60mL/min, and introducing N 2 After 30min, a xenon lamp of 300W is used as a simulated light source for irradiation, 10mL of sample is collected every 30min, nahner reagent is added, supernatant liquid is extracted after full reaction, and absorbance is tested by an ultraviolet spectrometer at a wavelength of 420 nm.
800-CaCuSi was measured by the method described above 4 O 10 NH after 120min 4 + The production rate reaches 58.47 mu mol g -1 ·h -1 。
CaCuSi obtained when the calcination temperature in step (2) is 1000℃as measured by the above method 4 O 10 NH after 120min 4 + The production rate reaches 60.32 mu mol g -1 ·h -1 。
Example 2
(1) 5g of attapulgite powder and ammonium sulfate are mixed according to the mass ratio of 1:2 mixing and placing the mixture into a ceramic crucible, placing the crucible into a muffle furnace, heating to 500 ℃ at a speed of 2 ℃/min, naturally cooling to room temperature, and obtaining a calcined product according to a solid-to-liquid ratio of 1:20 are dispersed into 2mol/L hydrochloric acid solution, solid is separated out after being stirred for 6 hours under 80 ℃ in a hydrothermal mode, and white SiO is obtained after washing and drying 2 And (3) powder.
(2) 1.11g Cu 2 (OH) 2 CO 3 And 1.0g eggshell powder to obtain 1.2g SiO 2 Placing the powder and the mixture in a crucible, transferring the crucible into a muffle furnace, calcining for 2 hours at 850 ℃, naturally cooling to room temperature, grinding and drying to obtain 850-CaCuSi 4 O 10 。
Subsequent detection is as in example 1, NH after 120min 4 + The production rate reaches 86.88 mu mol g -1 ·h -1 。
Example 3
(1) 5g of attapulgite powder and ammonium sulfate are mixed according to the mass ratio of 1:3 mixing and placing the mixture in a ceramic crucible, placing the crucible in a muffle furnace, heating to 500 ℃ at a speed of 2 ℃/min, naturally cooling to room temperature, and obtaining a calcined product according to a solid-to-liquid ratio of 1:20 are dispersed into 2mol/L hydrochloric acid solution, and are subjected to hydrothermal stirring at 80 ℃ for 6 hours and then separatedSeparating out solid, washing and drying to obtain white SiO 2 And (3) powder.
(2) 1.11g Cu 2 (OH) 2 CO 3 And 1.8g of prepared SiO from 1.0g of eggshell powder 2 Placing the powder and the mixture in a crucible, transferring to a muffle furnace, calcining for 2h at 900 ℃, naturally cooling to room temperature, grinding and drying to obtain 900-CaCuSi 4 O 10 。
Subsequent detection is as in example 1, NH after 120min 4 + The production rate reaches 124.68 mu mol g -1 ·h -1
Example 4
(1) 5g of attapulgite powder and ammonium sulfate are mixed according to the mass ratio of 1:4 mixing and placing the mixture into a ceramic crucible, placing the crucible into a muffle furnace, heating to 500 ℃ at a speed of 2 ℃/min, naturally cooling to room temperature, and obtaining a calcined product according to a solid-to-liquid ratio of 1:20 are dispersed into 2mol/L hydrochloric acid solution, solid is separated out after being stirred for 6 hours under 80 ℃ in a hydrothermal mode, and white SiO is obtained after washing and drying 2 And (3) powder.
(2) 1.11g Cu 2 (OH) 2 CO 3 And 1.0g eggshell powder 2.4g of the obtained SiO 2 Placing the powder and the mixture in a crucible, transferring the crucible into a muffle furnace, calcining for 2h at 950 ℃, naturally cooling to room temperature, grinding and drying to obtain 950-CaCuSi 4 O 10 。
Subsequent detection is as in example 1, NH after 120min 4 + The production rate reaches 107.96 mu mol g -1 ·h -1 。
Example 5
(1) 5g of attapulgite powder and ammonium sulfate are mixed according to the mass ratio of 1:5 mixing and placing the mixture in a ceramic crucible, placing the crucible in a muffle furnace, heating to 500 ℃ at a speed of 2 ℃/min, naturally cooling to room temperature, and obtaining a calcined product according to a solid-to-liquid ratio of 1:20 are dispersed into 2mol/L hydrochloric acid solution, solid is separated out after being stirred for 6 hours under 80 ℃ in a hydrothermal mode, and white SiO is obtained after washing and drying 2 And (3) powder.
(2) 1.11g Cu 2 (OH) 2 CO 3 And 1.0g eggshell powder to obtain 3.0g SiO 2 Placing the powder and the mixture in a crucible, transferring to a muffle furnace, calcining for 2h at 1000 ℃, naturally cooling to room temperature, grinding and drying to obtain 1000-CaCuSi 4 O 10 。
Subsequent detection is as in example 1, NH after 120min 4 + The production rate reaches 78.45 mu mol g -1 ·h -1 。
Comparative example 1
(1) 5g of attapulgite powder and ammonium sulfate are mixed according to the mass ratio of 1:1, mixing and placing the mixture into a ceramic crucible, placing the crucible into a muffle furnace, heating to 500 ℃ at a speed of 2 ℃/min, then naturally cooling to room temperature, and obtaining a calcined product according to a solid-to-liquid ratio of 1:20 are dispersed into 2mol/L hydrochloric acid solution, solid is separated out after being stirred for 6 hours under 80 ℃ in a hydrothermal mode, and white SiO is obtained after washing and drying 2 And (3) powder.
(2) 2.4g of the prepared SiO was taken 2 Powder and 1.11g Cu 2 (OH) 2 CO 3 Mixing, placing in a crucible, transferring into a muffle furnace, calcining at 800 deg.C for 2 hr, naturally cooling to room temperature, grinding, and oven drying to obtain CuSiO 3 。
Subsequent detection is as in example 1, NH after 120min 4 + The production rate is only 27.36 mu mol g -1 ·h -1 So there is no photo-response in the near infrared region, resulting in CuSiO in the same case 3 The photocatalytic nitrogen fixation effect is weaker than CaCuSi 4 O 10 。
Comparative example 2
(1) 5g of attapulgite powder and ammonium sulfate are mixed according to the mass ratio of 1:1, mixing and placing the mixture into a ceramic crucible, placing the crucible into a muffle furnace, heating to 500 ℃ at a speed of 2 ℃/min, then naturally cooling to room temperature, and obtaining a calcined product according to a solid-to-liquid ratio of 1:20 are dispersed into 2mol/L hydrochloric acid solution, solid is separated out after being stirred for 6 hours under 80 ℃ in a hydrothermal mode, and white SiO is obtained after washing and drying 2 And (3) powder.
(2) 2.4g of the prepared SiO was taken 2 The powder was mixed with 1.0g eggshell powder and placed in a crucible and transferred to a muffle furnaceCalcining at 800 deg.c for 2 hr, cooling naturally to room temperature, grinding and stoving to obtain CaSiO 3 。
Subsequent detection is as in example 1, NH after 120min 4 + The production rate only reaches 33.42 mu mol g -1 ·h -1 。
The foregoing is only a preferred embodiment of the present application, but the scope of the present application is not limited thereto, and any person skilled in the art, who is within the scope of the present application, should make equivalent substitutions or modifications according to the technical scheme and the concept of the present application, and should be covered by the scope of the present application.
Claims (9)
1. The application of the calcium copper silicate material prepared by using attapulgite and biomass is characterized in that:
the preparation of the calcium silicate copper material by using the attapulgite and biomass comprises the following steps:
(1) Mixing attapulgite powder and ammonium salt in a mass ratio of 1:1-1:5, placing the mixture into a ceramic crucible, placing the crucible into a muffle furnace, heating to 400-700 ℃ at a speed of 1-8 ℃/min, naturally cooling to room temperature, dispersing the obtained calcined product into an acid solution, hydrothermally stirring for 1-5 h, separating out solids, washing, and drying to obtain white SiO 2 A powder;
(2) Mixing basic cupric carbonate and biomass containing calcium salt with SiO prepared in step (1) 2 The powder is prepared from the following components in percentage by mole (0.5-1): 0.5-1: mixing the materials according to a feeding ratio of 0.5-5, calcining for 1-5 h at 800-1000 ℃, naturally cooling to room temperature, grinding and drying to obtain the calcium copper silicate material;
the application refers to the use for photocatalytic synthesis of ammonia.
2. The use of the calcium copper silicate material prepared from attapulgite and biomass according to claim 1, wherein: the temperature rising speed in the step (1) is 2 ℃/min, and the temperature rises to 500 ℃.
3. The use of the calcium copper silicate material prepared from attapulgite and biomass according to claim 1, wherein: the acid solution in the step (1) is hydrochloric acid solution, the concentration of the hydrochloric acid solution is 2mol/L, the solid-to-liquid ratio of the calcined product to the hydrochloric acid is 1:20, and the temperature of hydrothermal stirring is 80 ℃.
4. The use of the calcium copper silicate material prepared from attapulgite and biomass according to claim 1, wherein: the biomass containing calcium salt in the step (2) is eggshell powder and/or shell powder.
5. The use of the calcium copper silicate material prepared from attapulgite and biomass according to claim 1, wherein: the calcination time described in step (2) was 2 h.
6. The use of the calcium copper silicate material prepared from attapulgite and biomass according to claim 1, wherein: the method comprises the following steps: dispersing the calcium silicate copper material in deionized water, then adding the deionized water into a photocatalytic reaction device, and introducing N 2 And carrying out photocatalysis by illumination to obtain ammonia.
7. The use of the calcium copper silicate material prepared from attapulgite and biomass according to claim 1, wherein: and (3) dispersing the obtained calcined product in the step (1) into hydrochloric acid solution and carrying out hydrothermal stirring for 1-5 h, wherein the hydrothermal stirring method is mechanical stirring or magnetic stirring.
8. The use of the calcium copper silicate material prepared from attapulgite and biomass according to claim 1, wherein: the ammonium salt in the step (1) is ammonium sulfate, ammonium nitrate or basic ammonium carbonate.
9. The use of the calcium copper silicate material prepared from attapulgite and biomass according to claim 1, wherein: the acid solution in the step (1) is hydrochloric acid, sulfuric acid or nitric acid solution.
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