CN107352554B - Preparation method and application of magnetic X-type molecular sieve - Google Patents
Preparation method and application of magnetic X-type molecular sieve Download PDFInfo
- Publication number
- CN107352554B CN107352554B CN201710642378.5A CN201710642378A CN107352554B CN 107352554 B CN107352554 B CN 107352554B CN 201710642378 A CN201710642378 A CN 201710642378A CN 107352554 B CN107352554 B CN 107352554B
- Authority
- CN
- China
- Prior art keywords
- molecular sieve
- magnetic
- type molecular
- coal gangue
- 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.)
- Expired - Fee Related
Links
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B39/00—Compounds having molecular sieve and base-exchange properties, e.g. crystalline zeolites; Their preparation; After-treatment, e.g. ion-exchange or dealumination
- C01B39/02—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof; Direct preparation thereof; Preparation thereof starting from a reaction mixture containing a crystalline zeolite of another type, or from preformed reactants; After-treatment thereof
- C01B39/20—Faujasite type, e.g. type X or Y
- C01B39/22—Type X
-
- 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
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
- B01J20/10—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising silica or silicate
- B01J20/16—Alumino-silicates
- B01J20/18—Synthetic zeolitic molecular sieves
-
- 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
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/28—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
- B01J20/28002—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their physical properties
- B01J20/28009—Magnetic 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
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/28—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
- B01J20/28054—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their surface properties or porosity
- B01J20/28057—Surface area, e.g. B.E.T specific surface area
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/28—Treatment of water, waste water, or sewage by sorption
- C02F1/281—Treatment of water, waste water, or sewage by sorption using inorganic sorbents
-
- 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
- C01P2002/00—Crystal-structural characteristics
- C01P2002/80—Crystal-structural characteristics defined by measured data other than those specified in group C01P2002/70
- C01P2002/85—Crystal-structural characteristics defined by measured data other than those specified in group C01P2002/70 by XPS, EDX or EDAX data
-
- 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
- C01P2004/03—Particle morphology depicted by an image obtained by SEM
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/10—Inorganic compounds
- C02F2101/20—Heavy metals or heavy metal compounds
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Inorganic Chemistry (AREA)
- Analytical Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Geology (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Materials Engineering (AREA)
- Hydrology & Water Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
- Hard Magnetic Materials (AREA)
- Compounds Of Iron (AREA)
Abstract
The invention discloses a preparation method and application of a magnetic X-type molecular sieve, which comprises the steps of grinding coal gangue, and roasting and activating the coal gangue at high temperature by using sodium carbonate; oxidizing at low temperature, adding hydrochloric acid, soaking at 90 deg.C, filtering, and adding oxalic acid into the filtrate; washing the solid, drying, adding sodium hydroxide solid, grinding to be uniformly mixed, and carrying out alkali fusion at low temperature; adding deionized water and citric acid, aging at 60 deg.C, adding the above filtrate, and ultrasonic crystallizing to synthesize iron-doped molecular sieve; and (3) placing the iron-doped molecular sieve sample in a tubular furnace, and reducing at high temperature to obtain the magnetic X-type molecular sieve. The magnetic X-type molecular sieve prepared by the invention has the advantages of high specific surface area and strong adsorption performance, the solid-liquid separation of the product is easy through an external magnetic field, the problem of high cost synthesis of the molecular sieve is solved, a new way is provided for recycling, refining and efficient utilization of coal gangue, the effect of changing waste into valuable is achieved, and the requirements of environmental protection and low carbon are met.
Description
Technical Field
The invention belongs to the technical field of preparation of X-type molecular sieves, and particularly relates to a preparation method and application of a magnetic X-type molecular sieve.
Background
The coal gangue is solid waste discharged in the coal mining and coal dressing processes, is a black and gray rock with lower carbon content and harder than coal and is associated with a coal bed in the coal forming process, and the output is large. At present, the application of the coal gangue is mainly limited in the fields of building industry, energy industry, agriculture and the like, the utilization level and the proportion are low, and the accumulation of the coal gangue not only affects the environment, but also occupies a large amount of land. The molecular sieve prepared by the method can reduce pollution, expand the raw material sources of the molecular sieve, increase the added value of the molecular sieve and expand the utilization way of coal gangue. Molecular sieves are of two types, natural and synthetic: natural molecular sieves are mostly formed from the reaction of volcanic tuff and sedimentary rock in the sea or lake phase. At present, more than 1000 kinds of zeolite ores are found in the world, and more important are 35 kinds; the synthetic molecular sieve comes out from the 50 th of the 20 th century, greatly makes up for the deficiency of natural molecular sieve resources, and becomes the main force of the molecular sieve market.
The X-type molecular sieve has excellent performance and is widely applied to industry. However, the directly prepared X-type molecular sieve is generally nano or micron powder, which makes it difficult to separate from the liquid phase of the working fluid system. The patent utilizes the coal gangue in the clarified mining area to prepare the magnetic X-shaped molecular sieve, and Fe of the magnetic X-shaped molecular sieve is obtained after calcination2O3The content reaches 10.10%, and the iron in the prepared magnetic X-type molecular sieve is directly converted into magnetic iron without adding iron. The magnetic X-type molecular sieve prepared from coal gangue not only has the excellent performance of the molecular sieve, but also is endowed with magnetism, thereby being beneficial to separation from the working solution.
Disclosure of Invention
The technical problem to be solved by the invention is to provide a preparation method and application of a magnetic X-type molecular sieve aiming at the defects of the prior art. The invention uses the coal gangue for preparing the magnetic molecular sieve and provides a new process for preparing the magnetic molecular sieve by using the coal gangue, which not only solves the problem of high cost of molecular sieve synthesis, but also provides a new way for recycling, refining and efficiently utilizing the coal gangue, achieves the effect of changing waste into valuable and meets the requirements of environmental protection and low carbon.
In order to solve the problems, the invention adopts the technical scheme that:
a preparation method of a magnetic X-type molecular sieve comprises the following steps:
1) grinding the coal gangue into fine powder, adding sodium carbonate, roasting at 880-900 ℃, fully reacting and grinding to obtain a pretreated sample; wherein the mass ratio of the coal gangue powder to the sodium carbonate is (2-3) to 1;
2) oxidizing the pretreated coal gangue powder at 350-400 ℃, adding hydrochloric acid, soaking at 90-100 ℃, filtering to obtain filtered solid and filtrate, and adding oxalic acid into the filtrate for later use; wherein, oxalic acid and filterFe in liquid3+The molar ratio is 4-6;
3) washing and drying the solid obtained in the step 2), adding sodium hydroxide solid according to the mass ratio of 1:1, grinding until the sodium hydroxide solid is uniformly mixed, and carrying out alkali fusion at the temperature of 450-500 ℃; then adding deionized water and citric acid, carrying out aging reaction, and mixing the citric acid with Al in the solution2O3The molar ratio of (A) to (B) is 0.65-0.85; finally, adding the standby filtrate obtained in the step 2), and synthesizing the iron-doped molecular sieve by ultrasonic crystallization;
4) and (2) placing the synthesized iron-doped molecular sieve in a tubular furnace, introducing nitrogen to completely exhaust air, stopping introducing nitrogen, heating, introducing hydrogen, performing reduction reaction after the temperature is raised to 650-700 ℃, introducing nitrogen and then closing hydrogen after full reaction, cooling a sample to room temperature and then closing nitrogen to prepare the magnetic X-type molecular sieve.
In the step 1), the coal gangue is ground into 300-325 meshes and then added with sodium carbonate.
In the step 2), the mass concentration of the hydrochloric acid is 15%.
In the step 2), 0.450g to 0.675g of oxalic acid is correspondingly added into each gram of coal gangue.
In the step 3), the temperature of ultrasonic crystallization is 75-95 ℃, and the time is 6-10 h.
In the step 3), the aging reaction temperature is 60-70 ℃ and the time is 4-5 h.
In the step 4), the reduction reaction time is 2-3 h.
In the step 4), the introduction flow rate of the hydrogen is 50cm3/min。
The prepared magnetic X-type molecular sieve is applied to adsorbing heavy metal ions in wastewater. Especially for adsorbing lead ions in wastewater.
Compared with the prior art, the invention has the following advantages:
after grinding the coal gangue, roasting the coal gangue at high temperature by using sodium carbonate to activate the coal gangue; oxidizing at low temperature, adding hydrochloric acid, soaking at 90 deg.C, filtering, and adding oxalic acid into the filtrate; washing the solid, drying, adding sodium hydroxide solid, grinding to be uniformly mixed, and carrying out alkali fusion at low temperature; adding deionized water and citric acid, aging at 60 deg.C, adding the above filtrate, and ultrasonic crystallizing to synthesize iron-doped molecular sieve; and (3) placing the iron-doped molecular sieve sample in a tubular furnace, and reducing at high temperature to obtain the magnetic X-type molecular sieve. The magnetic X-type molecular sieve is prepared by adopting coal gangue as a raw material, dissolving iron in hydrochloric acid under ultrasonic waves, adding oxalic acid for complexing iron, and finally reducing at high temperature. Greatly reduces the preparation and application cost of the molecular sieve. In the preparation process, the coal gangue is used as a raw material, the citric acid and the oxalic acid which are added as auxiliary agents are added, and ultrasonic vibration heating is carried out, so that the reaction time is greatly shortened, the crystallization temperature is reduced, and the energy consumption is saved; meanwhile, the utilization rate of the molecular sieve is improved by utilizing magnetic separation, the method has strong commercial competitiveness and can greatly promote the rapid development of the molecular sieve in China.
The invention can effectively solve the problem that the reaction liquid is difficult to separate in the application of the molecular sieve. By the experiment of lead ion adsorption, the adsorption rate of the magnetic molecular sieve is more than 94%, and the magnetic molecular sieve is easily separated from reaction liquid by using an external magnetic field, so that the application of the magnetic molecular sieve in the adsorption industry is greatly improved. The magnetic X-type molecular sieve prepared by utilizing the coal gangue has the advantages of high crystallinity, uniform crystal distribution, uniform particle size, complete crystal form, regular crystal morphology, clear square edges and regular octahedron shape.
Drawings
FIG. 1 is an XRD pattern of a magnetic type X molecular sieve prepared in example 1 of the present invention;
FIG. 2 is an SEM picture of the magnetic X-type molecular sieve prepared in example 1 of the present invention.
FIG. 3 is an X photoelectron spectrum of the magnetic X-type molecular sieve prepared in example 1 of the present invention;
FIG. 4 is an IR spectrum of the magnetic X-type molecular sieve prepared in example 2 of the present invention.
Detailed Description
The invention relates to a preparation method of a magnetic X-type molecular sieve, which comprises the following steps:
step one, grinding the coal gangue to 300-325 meshes, placing the coal gangue in an ash pan, then adding sodium carbonate into the ash pan, roasting for 2-3 h at the temperature of 880-900 ℃, and grinding to obtain a pretreated sample; the mass ratio of the coal gangue to the sodium carbonate is (2-3) to 1;
secondly, oxidizing the pretreated coal gangue powder at 350-400 ℃ for 1.5-2H, adding hydrochloric acid with the mass concentration of 15%, soaking at 90-100 ℃ for 2-3H, filtering, and adding H into the filtrate2C2O4/Fe3+Oxalic acid with the molar ratio of 4-6 for later use; wherein, 0.450 g-0.675 gH is correspondingly added into each gram of coal gangue2C2O4;
Step three, after the solid in the step two is washed, adding sodium hydroxide solid according to the mass ratio of 1:1, grinding the mixture until the mixture is uniformly mixed, carrying out alkali fusion at the temperature of 450-500 ℃ for 1.5-2 h, and adding deionized water and C6H8O7/Al2O3Aging citric acid with the molar ratio of 0.65-0.85 for 4-5 h at the temperature of 60-70 ℃; then adding the standby filtrate, and carrying out ultrasonic crystallization at the temperature of 75-95 ℃ for 6-10 h to synthesize the iron-doped molecular sieve;
step four, placing the synthesized iron-doped molecular sieve sample in a small porcelain boat, placing the porcelain boat in a tube furnace, connecting two ends of a furnace core with rubber plugs with rubber tubes, opening a nitrogen valve to introduce nitrogen, discharging air in the tube furnace after 1-1.5 hours, switching on a power supply to set the temperature at 650-700 ℃, simultaneously opening a hydrogen valve, closing the nitrogen valve, and controlling the flow at 50cm3And/min, reacting for 2-3 h when the temperature rises to the set temperature, introducing nitrogen, then closing hydrogen, cooling the sample to room temperature, and then closing nitrogen to prepare the magnetic X-type molecular sieve.
The technical solution of the present invention is further described in detail by the accompanying drawings and examples.
The coal gangue used in the embodiments 1 to 6 is coal gangue produced in a Chengji mining area in Shaanxi. The chemical composition (wt%) of the coal gangue is detected to be shown in table 1:
TABLE 1
Components | SiO2 | Al2O3 | Fe2O3 | CaO | MgO |
Weight content (%) | 58.80 | 25.61 | 10.10 | 2.09 | 0.21 |
Example 1
The preparation of the magnetic X-type molecular sieve by using the coal gangue comprises the following steps:
step one, grinding coal gangue to 325 meshes, placing the powder into an ash pan, adding 1: 3 of coal gangue and sodium carbonate into the ash pan, roasting for 2 hours at the temperature of 900 ℃, and grinding to obtain a pretreated sample;
step two, oxidizing the pretreated coal gangue powder at 350 ℃ for 2H, adding hydrochloric acid with the mass concentration of 15%, soaking at 90 ℃ for 2H, filtering, and adding H into the filtrate2C2O4/Fe3+Oxalic acid with the molar ratio of 4 for standby;
step threeWashing the solid obtained in the step two, adding sodium hydroxide solid according to the mass ratio of 1:1, grinding until the sodium hydroxide solid is uniformly mixed, carrying out alkali fusion for 2h at 450 ℃, and adding deionized water and C6H8O7/Al2O3Aging citric acid with a molar ratio of 0.65 at 70 deg.C for 4 hr; and adding the filtrate for later use, and performing ultrasonic crystallization at the temperature of 75 ℃ for 10 hours to synthesize the iron-doped molecular sieve.
Step four, placing the synthesized iron-doped molecular sieve sample in a small porcelain boat, placing the porcelain boat in a tube furnace, connecting two ends of a furnace core with rubber plugs with rubber tubes, opening a nitrogen valve to introduce nitrogen, after 1 hour, after the air in the tube furnace is completely discharged, switching on a power supply, setting the temperature to be 650 ℃, simultaneously opening a hydrogen valve, closing the nitrogen valve, and controlling the flow to be 50cm3And/min, reacting for 2h when the temperature rises to the set temperature, introducing nitrogen, closing hydrogen, cooling the sample to room temperature, and closing nitrogen to prepare the magnetic X-type molecular sieve.
The magnetic X-type molecular sieve prepared in this example was characterized by XRD, SEM and XPS, and the results are shown in fig. 1 to 3. Fig. 1 is an XRD pattern of the magnetic X-type molecular sieve prepared in example 1, and it can be seen from the XRD pattern of the magnetic X-type molecular sieve prepared in this example is consistent with the XRD pattern (JCPDS card No.38.0237) of the standard NaX-type molecular sieve, that is, strong diffraction peaks appear around 15.70, 23.66, 27.04, and 31.36, respectively, in 2 θ. From the whole XRD pattern, the diffraction peak is sharp and has large intensity, which indicates that the product has high crystallization degree.
Fig. 2 is an SEM photograph of the magnetic X-type molecular sieve prepared in this example, and the product has high crystallinity, uniform crystal distribution, uniform particle size, clear crystal grains, complete crystal form, regular crystal morphology, and clear square edges, and the crystal grains are octahedral. FIG. 3 is an X photoelectron spectrum of a magnetic X-type molecular sieve, in which the spectral lines clearly show Si2p、A12p、OlsAnd NalsThe equipeaks show that elements such as Si, Al, O, Na and the like exist on the surface of the magnetic molecular sieve, and weak Fe appears in a spectral line2pThe peak shows that Fe exists on the surface, and the calculation shows that Fe on the surface of the magnetic molecular sieve3O4The content is 2.60% by mass in combination with the above chemical analysisIt shows that the iron entering the molecular sieve by isomorphous replacement is unstable, and basically generates Fe under the condition of high-temperature reduction3O4In addition, the magnetic molecular sieve prepared by the method is also shown, and the generated Fe3O4In admixture with the molecular sieve formed.
The adsorption performance of the magnetic X-type molecular sieve prepared by the implementation on lead ions in wastewater is measured by a spectrophotometry, and the measured adsorption rate reaches 94.2%.
Example 2
The preparation of the magnetic X-type molecular sieve by using the coal gangue comprises the following steps:
step one, grinding coal gangue to 325 meshes, placing the powder into an ash pan, adding 1: 3 of coal gangue and sodium carbonate into the ash pan, roasting for 2 hours at the temperature of 900 ℃, and grinding to obtain a pretreated sample;
step two, oxidizing the pretreated coal gangue powder at 350 ℃ for 2H, adding hydrochloric acid with the mass concentration of 15%, soaking at 90 ℃ for 2H, filtering, and adding H into the filtrate2C2O4/Fe3+Oxalic acid with the molar ratio of 6 for standby;
step three, after the solid in the step two is washed, adding sodium hydroxide solid according to the mass ratio of 1:1, grinding the mixture until the mixture is uniformly mixed, carrying out alkali fusion for 2 hours at the temperature of 450 ℃, and adding deionized water and C6H8O7/Al2O3Aging citric acid with a molar ratio of 0.75 at 60 deg.C for 5 hr; and adding the standby filtrate, and performing ultrasonic crystallization at the temperature of 75 ℃ for 6 hours to synthesize the iron-doped molecular sieve.
Step four, placing the synthesized iron-doped molecular sieve sample in a small porcelain boat, placing the porcelain boat in a tube furnace, connecting two ends of a furnace core with rubber plugs with rubber tubes, opening a nitrogen valve to introduce nitrogen, after 1 hour, after the air in the tube furnace is completely discharged, switching on a power supply, setting the temperature to be 650 ℃, simultaneously opening a hydrogen valve, closing the nitrogen valve, and controlling the flow to be 50cm3And/min, reacting for 2h when the temperature rises to the set temperature, introducing nitrogen, closing hydrogen, cooling the sample to room temperature, and closing nitrogen to prepare the magnetic X-type molecular sieve.
The adsorption performance of the magnetic X-type molecular sieve prepared by the implementation on lead ions in wastewater is measured by a spectrophotometry, and the measured adsorption rate reaches 94.6%.
Example 3
The preparation of the magnetic X-type molecular sieve by using the coal gangue comprises the following steps:
step one, grinding coal gangue to 325 meshes, placing the powder into an ash pan, adding 1: 3 of coal gangue and sodium carbonate into the ash pan, roasting for 2 hours at the temperature of 900 ℃, and grinding to obtain a pretreated sample;
step two, oxidizing the pretreated coal gangue powder at 350 ℃ for 2H, adding hydrochloric acid with the mass concentration of 15%, soaking at 90 ℃ for 2H, filtering, and adding H into the filtrate2C2O4/Fe3+Oxalic acid with the molar ratio of 5 for standby;
step three, after the solid in the step two is washed, adding sodium hydroxide solid according to the mass ratio of 1:1, grinding the mixture until the mixture is uniformly mixed, carrying out alkali fusion for 2 hours at the temperature of 450 ℃, and adding deionized water and C6H8O7/Al2O3Aging citric acid with a molar ratio of 0.85 at 70 deg.C for 4 hr; and adding the standby filtrate, and carrying out ultrasonic crystallization at the temperature of 85 ℃ for 8 hours to synthesize the iron-doped molecular sieve.
Step four, placing the synthesized iron-doped molecular sieve sample in a small porcelain boat, placing the porcelain boat in a tube furnace, connecting two ends of a furnace core with rubber plugs with rubber tubes, opening a nitrogen valve to introduce nitrogen, after 1 hour, after the air in the tube furnace is completely discharged, switching on a power supply, setting the temperature to be 650 ℃, simultaneously opening a hydrogen valve, closing the nitrogen valve, and controlling the flow to be 50cm3And/min, reacting for 2h when the temperature rises to the set temperature, introducing nitrogen, closing hydrogen, cooling the sample to room temperature, and closing nitrogen to prepare the magnetic X-type molecular sieve.
The adsorption performance of the magnetic X-type molecular sieve prepared by the implementation on lead ions in wastewater is measured by a spectrophotometry, and the measured adsorption rate reaches 94.5%.
Example 4
The preparation of the magnetic X-type molecular sieve by using the coal gangue comprises the following steps:
step one, grinding coal gangue to 325 meshes, placing the powder into an ash pan, adding 1: 3 of coal gangue and sodium carbonate into the ash pan, roasting for 2 hours at the temperature of 900 ℃, and grinding to obtain a pretreated sample;
step two, oxidizing the pretreated coal gangue powder at 350 ℃ for 2H, adding hydrochloric acid with the mass concentration of 15%, soaking at 90 ℃ for 2H, filtering, and adding H into the filtrate2C2O4/Fe3+Oxalic acid with the molar ratio of 5 for standby;
step three, after the solid in the step two is washed, adding sodium hydroxide solid according to the mass ratio of 1:1, grinding the mixture until the mixture is uniformly mixed, carrying out alkali fusion for 2 hours at the temperature of 450 ℃, and adding deionized water and C6H8O7/Al2O3Aging citric acid with a molar ratio of 0.65 at 70 deg.C for 4 hr; and adding the filtrate for later use, and performing ultrasonic crystallization at the temperature of 95 ℃ for 8 hours to synthesize the iron-doped molecular sieve.
Step four, placing the synthesized iron-doped molecular sieve sample in a small porcelain boat, placing the porcelain boat in a tube furnace, connecting two ends of a furnace core with rubber plugs with rubber tubes, opening a nitrogen valve to introduce nitrogen, after 1 hour, after the air in the tube furnace is completely discharged, switching on a power supply, setting the temperature to 700 ℃, simultaneously opening a hydrogen valve, closing the nitrogen valve, and controlling the flow to be 50cm3And/min, reacting for 2h when the temperature rises to the set temperature, introducing nitrogen, closing hydrogen, cooling the sample to room temperature, and closing nitrogen to prepare the magnetic X-type molecular sieve.
The adsorption performance of the magnetic X-type molecular sieve prepared by the implementation on lead ions in wastewater is measured by a spectrophotometry, and the measured adsorption rate reaches 95.1%.
Example 5
The preparation of the magnetic X-type molecular sieve by using the coal gangue comprises the following steps:
step one, grinding coal gangue to 325 meshes, placing the powder into an ash pan, adding 1: 3 of coal gangue and sodium carbonate into the ash pan, roasting for 2 hours at the temperature of 900 ℃, and grinding to obtain a pretreated sample;
step two, oxidizing the pretreated coal gangue powder at 350 ℃ for 2h, adding hydrochloric acid with the mass concentration of 15 percent into the oxidized coal gangue powderSoaking at 90 deg.C for 2 hr, filtering, and adding H into the filtrate2C2O4/Fe3+Oxalic acid with the molar ratio of 5 for standby;
step three, after the solid in the step two is washed, adding sodium hydroxide solid according to the mass ratio of 1:1, grinding the mixture until the mixture is uniformly mixed, carrying out alkali fusion for 2 hours at the temperature of 450 ℃, and adding deionized water and C6H8O7/Al2O3Aging citric acid with a molar ratio of 0.75 at 60 deg.C for 3 h; and adding the standby filtrate, and carrying out ultrasonic crystallization at the temperature of 85 ℃ for 8 hours to synthesize the iron-doped molecular sieve.
Step four, placing the synthesized iron-doped molecular sieve sample in a small porcelain boat, placing the porcelain boat in a tube furnace, connecting two ends of a furnace core with rubber plugs with rubber tubes, opening a nitrogen valve to introduce nitrogen, after 1 hour, after the air in the tube furnace is completely discharged, switching on a power supply, setting the temperature to be 650 ℃, simultaneously opening a hydrogen valve, closing the nitrogen valve, and controlling the flow to be 50cm3And/min, reacting for 2h when the temperature rises to the set temperature, introducing nitrogen, closing hydrogen, cooling the sample to room temperature, and closing nitrogen to prepare the magnetic X-type molecular sieve.
The adsorption performance of the magnetic X-type molecular sieve prepared by the implementation on lead ions in wastewater is measured by a spectrophotometry, and the measured adsorption rate reaches 94.9%.
Example 6
The preparation of the magnetic X-type molecular sieve by using the coal gangue comprises the following steps:
step one, grinding coal gangue to 325 meshes, placing the powder into an ash pan, adding 1: 3 of coal gangue and sodium carbonate into the ash pan, roasting for 2 hours at the temperature of 900 ℃, and grinding to obtain a pretreated sample;
step two, oxidizing the pretreated coal gangue powder at 350 ℃ for 2H, adding hydrochloric acid with the mass concentration of 15%, soaking at 90 ℃ for 2H, filtering, and adding H into the filtrate2C2O4/Fe3+Oxalic acid with the molar ratio of 5 for standby;
step three, after the solid in the step two is washed, adding sodium hydroxide solid according to the mass ratio of 1:1, grinding the mixture until the mixture is uniformly mixed, carrying out alkali fusion for 2 hours at the temperature of 450 ℃, and adding deionized waterAnd C6H8O7/Al2O3Aging citric acid with a molar ratio of 0.85 at 70 deg.C for 3 hr; and adding the standby filtrate, and performing ultrasonic crystallization at the temperature of 95 ℃ for 6 hours to synthesize the iron-doped molecular sieve.
Step four, placing the synthesized iron-doped molecular sieve sample in a small porcelain boat, placing the porcelain boat in a tube furnace, connecting two ends of a furnace core with rubber plugs with rubber tubes, opening a nitrogen valve to introduce nitrogen, after 1 hour, after the air in the tube furnace is completely discharged, switching on a power supply, setting the temperature to be 650 ℃, simultaneously opening a hydrogen valve, closing the nitrogen valve, and controlling the flow to be 50cm3And/min, reacting for 2h when the temperature rises to the set temperature, introducing nitrogen, closing hydrogen, cooling the sample to room temperature, and closing nitrogen to prepare the magnetic X-type molecular sieve.
The adsorption performance of the magnetic X-type molecular sieve prepared by the implementation on lead ions in wastewater is measured by a spectrophotometry, and the measured adsorption rate reaches 95.5%.
The above description is only for the preferred embodiment of the present invention, and is not intended to limit the present invention in any way. Any simple modification, change and equivalent changes of the above embodiments according to the technical essence of the invention are still within the protection scope of the technical solution of the invention.
Claims (9)
1. The preparation method of the magnetic X-type molecular sieve is characterized by comprising the following steps of:
1) grinding the coal gangue into fine powder, adding sodium carbonate, roasting at 880-900 ℃, fully reacting and grinding to obtain a pretreated sample; wherein the mass ratio of the coal gangue powder to the sodium carbonate is (2-3) to 1;
2) oxidizing the pretreated coal gangue powder at 350-400 ℃, adding hydrochloric acid, soaking at 90-100 ℃ under ultrasonic wave, filtering to obtain filtered solid and filtrate, and adding oxalic acid into the filtrate for later use; wherein, the oxalic acid and the Fe in the filtrate3+The molar ratio is 4-6; adding 0.450 g-0.675 g oxalic acid into each gram of coal gangue;
3) washing and drying the solid obtained in the step 2), adding sodium hydroxide solid according to the mass ratio of 1:1, grinding until the mixture is uniformly mixed,alkali fusion at 450-500 deg.c; then adding deionized water and citric acid, carrying out aging reaction, and mixing the citric acid with Al in the solution2O3The molar ratio of (A) to (B) is 0.65-0.85; finally, adding the standby filtrate obtained in the step 2), and synthesizing the iron-doped molecular sieve by ultrasonic crystallization;
4) and (2) placing the synthesized iron-doped molecular sieve in a tubular furnace, introducing nitrogen to completely exhaust air, stopping introducing nitrogen, heating, introducing hydrogen, performing reduction reaction after the temperature is raised to 650-700 ℃, introducing nitrogen and then closing hydrogen after full reaction, cooling a sample to room temperature and then closing nitrogen to prepare the magnetic X-type molecular sieve.
2. The method for preparing a magnetic X-type molecular sieve according to claim 1, wherein in the step 1), sodium carbonate is added after the coal gangue is ground into 300-325 meshes.
3. The method for preparing a magnetic X-type molecular sieve according to claim 1, wherein the hydrochloric acid concentration in step 2) is 15% by mass.
4. The method for preparing the magnetic X-type molecular sieve according to claim 1, wherein in the step 3), the temperature of ultrasonic crystallization is 75-95 ℃ and the time is 6-10 h.
5. The method for preparing the magnetic X-type molecular sieve according to claim 1, wherein in the step 3), the aging reaction temperature is 60-70 ℃ and the time is 4-5 h.
6. The method for preparing the magnetic X-type molecular sieve according to claim 1, wherein in the step 4), the reduction reaction time is 2-3 h.
7. The method for preparing a magnetic X-type molecular sieve according to claim 1, wherein in the step 4), the flow rate of hydrogen is 50cm3/min。
8. Use of the magnetic X-type molecular sieve prepared by the preparation method of any one of claims 1 to 7 in adsorption of heavy metal ions in wastewater.
9. The use according to claim 8 for adsorbing lead ions in wastewater.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201710642378.5A CN107352554B (en) | 2017-07-31 | 2017-07-31 | Preparation method and application of magnetic X-type molecular sieve |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201710642378.5A CN107352554B (en) | 2017-07-31 | 2017-07-31 | Preparation method and application of magnetic X-type molecular sieve |
Publications (2)
Publication Number | Publication Date |
---|---|
CN107352554A CN107352554A (en) | 2017-11-17 |
CN107352554B true CN107352554B (en) | 2020-04-21 |
Family
ID=60286679
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201710642378.5A Expired - Fee Related CN107352554B (en) | 2017-07-31 | 2017-07-31 | Preparation method and application of magnetic X-type molecular sieve |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN107352554B (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111170332B (en) * | 2020-01-02 | 2021-06-22 | 淮阴工学院 | Method for preparing magnetic ZSM-5 zeolite by using clay and red mud as raw materials as slightly soluble agent |
US11918973B1 (en) * | 2022-08-22 | 2024-03-05 | Sinanen Zeomic Co., Ltd. | Heavy metal adsorbent, water purification material, and method of manufacturing heavy metal adsorbent |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1238305A (en) * | 1998-06-04 | 1999-12-15 | 中国石油化工总公司 | Process for synthesizing fine-grain octahedra zeolite |
CN1254681A (en) * | 1999-11-09 | 2000-05-31 | 复旦大学 | Processf or preparing X-zeolite from coal gangue |
CN1280956A (en) * | 2000-08-10 | 2001-01-24 | 复旦大学 | Process for preparing high-crystallinity X-type zeolite from coal gangue as raw material |
CN101219795A (en) * | 2008-02-02 | 2008-07-16 | 河北工业大学 | X type zeolite molecular sieve and method for producing the same |
CN103523796A (en) * | 2013-09-27 | 2014-01-22 | 上海绿强新材料有限公司 | Synthesis method and application of submicron X-type molecular sieve |
-
2017
- 2017-07-31 CN CN201710642378.5A patent/CN107352554B/en not_active Expired - Fee Related
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1238305A (en) * | 1998-06-04 | 1999-12-15 | 中国石油化工总公司 | Process for synthesizing fine-grain octahedra zeolite |
CN1254681A (en) * | 1999-11-09 | 2000-05-31 | 复旦大学 | Processf or preparing X-zeolite from coal gangue |
CN1280956A (en) * | 2000-08-10 | 2001-01-24 | 复旦大学 | Process for preparing high-crystallinity X-type zeolite from coal gangue as raw material |
CN101219795A (en) * | 2008-02-02 | 2008-07-16 | 河北工业大学 | X type zeolite molecular sieve and method for producing the same |
CN103523796A (en) * | 2013-09-27 | 2014-01-22 | 上海绿强新材料有限公司 | Synthesis method and application of submicron X-type molecular sieve |
Non-Patent Citations (3)
Title |
---|
煤矸石制备X型分子筛对氨氮吸附性能的研究;王茜等;《化工新型材料》;20120731;第40卷(第7期);全文 * |
超声波作用下膨润土合成X型分子筛研究;蒋月秀等;《非金属矿》;20110331;第34卷(第2期);第1.3节 * |
高铁高硅煤矸石制备P型分子筛;孔德顺等;《硅酸盐通报》;20130630;第32卷(第6期);2.4节 * |
Also Published As
Publication number | Publication date |
---|---|
CN107352554A (en) | 2017-11-17 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN107285341B (en) | Method for preparing magnetic P-type molecular sieve by using coal gangue | |
US9422167B2 (en) | Method for forming basic nickel carbonate | |
CN109569545B (en) | Method for preparing aluminum-silicon porous material from fly ash | |
CN103551201B (en) | A kind of preparation method of copper hydroxyphosphate catalyst | |
CN108928834B (en) | MCM-41 mesoporous molecular sieve, and preparation method and application thereof | |
CN109603856B (en) | Method for preparing Erdite rod-shaped particles from wastewater and applying Erdite rod-shaped particles to water treatment | |
CN103571334A (en) | Cerium oxide polishing powder and preparation method thereof | |
WO2017101746A1 (en) | Bauxite desiliconization method | |
CN101007656A (en) | Waste molybdenum nickel cobalt catalyst utilization method for environmental protection | |
CN107352554B (en) | Preparation method and application of magnetic X-type molecular sieve | |
CN101306819B (en) | Process for abstracting white carbon black from fly ash or slag | |
CN102732214A (en) | Ceramic corundum abrasive containing multiphase additive | |
CN109485062A (en) | A kind of low temperature preparation method of lithium slag base NaA molecular sieve | |
CN108658092B (en) | Method for preparing P-type molecular sieve and high-silicon mordenite from aluminum residue extracted by fly ash acid method and utilization method of fly ash | |
CN112707428A (en) | Combined preparation method of nano calcium carbonate and pseudo-boehmite or white carbon black | |
CN103626222A (en) | Method for preparing micron-grade stannic oxide powder | |
CN106865565A (en) | A kind of flyash synthesizes the method for X-type zeolite | |
CN113845128A (en) | MOR zeolite molecular sieve and preparation method thereof | |
CN108946754B (en) | SBA-15 mesoporous molecular sieve, preparation method and application thereof, and method for producing alumina and SBA-15 mesoporous molecular sieve from fly ash | |
CN103803981A (en) | Method for preparing submicron silicon carbide powder | |
CN109665534A (en) | A method of mesopore silicon oxide is prepared using flyash acid leaching residue | |
CN103441315B (en) | Method for preparing manganese-zinc ferrite soft magnet by taking biological leachate of waste zinc-manganese battery as raw material | |
CN105110784A (en) | Method for preparing manganese zinc ferrite by using artificial rutile mother liquor | |
CN105271290B (en) | Method for preparing analcite through high-alumina fly ash | |
CN108502911B (en) | Barite purifying and whitening agent and purifying and whitening method thereof |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
GR01 | Patent grant | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20200421 Termination date: 20210731 |
|
CF01 | Termination of patent right due to non-payment of annual fee |