CN114950353A - High-activity-site molybdenum disulfide/carbon nanofiber aerogel adsorbent and preparation method thereof - Google Patents

High-activity-site molybdenum disulfide/carbon nanofiber aerogel adsorbent and preparation method thereof Download PDF

Info

Publication number
CN114950353A
CN114950353A CN202111399350.6A CN202111399350A CN114950353A CN 114950353 A CN114950353 A CN 114950353A CN 202111399350 A CN202111399350 A CN 202111399350A CN 114950353 A CN114950353 A CN 114950353A
Authority
CN
China
Prior art keywords
carbon nanofiber
aerogel
deionized water
molybdenum disulfide
adsorbent
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.)
Pending
Application number
CN202111399350.6A
Other languages
Chinese (zh)
Inventor
阮长平
赵冬敏
方媛
沈星灿
刘葵
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Guangxi Normal University
Original Assignee
Guangxi Normal University
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Guangxi Normal University filed Critical Guangxi Normal University
Priority to CN202111399350.6A priority Critical patent/CN114950353A/en
Publication of CN114950353A publication Critical patent/CN114950353A/en
Pending legal-status Critical Current

Links

Images

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/02Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
    • B01J20/0203Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising compounds of metals not provided for in B01J20/04
    • B01J20/0218Compounds of Cr, Mo, W
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/02Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
    • B01J20/0203Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising compounds of metals not provided for in B01J20/04
    • B01J20/0274Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising compounds of metals not provided for in B01J20/04 characterised by the type of anion
    • B01J20/0285Sulfides of compounds other than those provided for in B01J20/045
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/02Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
    • B01J20/20Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising free carbon; comprising carbon obtained by carbonising processes
    • B01J20/205Carbon nanostructures, e.g. nanotubes, nanohorns, nanocones, nanoballs
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/28Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
    • B01J20/28014Solid 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 form
    • B01J20/28047Gels
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/28Treatment of water, waste water, or sewage by sorption
    • C02F1/288Treatment of water, waste water, or sewage by sorption using composite sorbents, e.g. coated, impregnated, multi-layered
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2101/00Nature of the contaminant
    • C02F2101/10Inorganic compounds
    • C02F2101/20Heavy metals or heavy metal compounds
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/30Wastewater or sewage treatment systems using renewable energies
    • Y02W10/37Wastewater or sewage treatment systems using renewable energies using solar energy

Abstract

The invention belongs to the technical field of sewage treatment agents, and provides a molybdenum disulfide/carbon nanofiber aerogel adsorbent with high active sites and a preparation method thereof, wherein the method comprises the following steps: soaking and washing the cellulose acetate in deionized water, and then placing the cellulose acetate in a tubular furnace in a nitrogen protective atmosphere to heat to 400-700 ℃ for heat preservation to obtain black carbon nanofiber aerogel; weighing ammonium molybdate tetrahydrate and thiourea, adding deionized water, performing ultrasonic treatment until the ammonium molybdate tetrahydrate and the thiourea are completely dissolved, and uniformly stirring to obtain a mixed solution A; adding the mixed solution A and the carbon nanofiber aerogel into a polytetrafluoroethylene reaction kettle; reacting under a hydrothermal condition, and performing solid-liquid separation on the obtained product to obtain a crude sample B; and washing the crude sample B with deionized water, and putting the crude sample B into a freeze vacuum drier for drying to obtain a sample which is the aerogel adsorbent. The product obtained by the method has stronger chelation with metal ions and more adsorption sites, and has excellent treatment effect on the sewage containing mercury ions.

Description

High-activity-site molybdenum disulfide/carbon nanofiber aerogel adsorbent and preparation method thereof
Technical Field
The invention relates to the technical field of sewage treatment agents, in particular to a molybdenum disulfide/carbon nanofiber aerogel adsorbent with high active sites and a preparation method thereof.
Background
Mercury is one of the highly toxic heavy metal contaminants that can cause birth defects, brain damage and disease in humans and other species, and has long been a threat to public health and the environment. Mercury is not biodegradable and therefore can accumulate in organisms, threatening human health through the food chain. Therefore, research on designing and preparing the high-efficiency mercury adsorbent is concerned by researchers at home and abroad.
Currently, many conventional methods for removing heavy metal ions from wastewater have been developed, such as ion exchange, membrane separation, electrochemical treatment, chemical precipitation, and adsorption methods. Among them, the adsorption method has become a generally accepted choice due to its advantages of high removal efficiency, simple operation, wide applicability, high cost performance, etc. At present, common adsorbents such as activated carbon, zeolite, clay and the like are used for adsorbing heavy metal ions, however, due to low adsorption efficiency, difficulty in separation, difficulty in reuse and the like, the feasibility of practical application of the adsorbents is reduced. Therefore, it is necessary to prepare a mercury adsorbent with low cost, simple process and high efficiency.
To date, various sulfur-containing materials have been paired with Hg due to the strong soft-soft interaction between sulfur and mercury 2+ The ions have strong binding affinity and become a unique mercury ion adsorbent. Recently, thiol-functionalized metal organic frameworks, organic polymers, carbon nanotubes, etc. have been reported as Hg 2+ Ion adsorbents (J.colloid.Interf.Sci.2015,456: 22-31; ACS Sustainable chem.Eng.2018,6, 6175-. However, due to the low sulfur content of these materials orLow sulfur utilization, and still exhibit relatively low Hg 2+ Ion adsorption capacity, and many materials are subject to complex synthetic procedures and high synthetic costs, limiting the possibilities of these materials for large scale synthesis and application. Molybdenum disulfide (MoS) 2 ) As one of typical representatives of transition metal sulfides, the transition metal sulfides have the advantages of abundant sulfur atoms, unique layered structure, controllable interlayer spacing, large specific surface area and the like, and have great potential for removing heavy metals. However, currently MoS 2 There are still limitations in the application process, such as MoS 2 The polymer has poor dispersibility in water and is easy to aggregate, so that a large number of adsorption sites cannot be effectively utilized, and the adsorption capacity of the polymer is reduced. In addition, the separation and recovery difficulty of the powdery molybdenum disulfide is high when the powdery molybdenum disulfide is dispersed in water, and secondary pollution is easily caused. By mixing MoS 2 The nanosheet is assembled with other carriers with a net structure to form a three-dimensional composite material, so that the limitations can be effectively overcome, and the separating and recycling capacity of the adsorbent is improved.
Carbon-based aerogels consisting of interconnected three-dimensional (3D) networks have attracted considerable attention due to their low cost, low density, high conductivity, porosity and specific surface area. The CNF aerogel produced by pyrolyzing BC belongs to one of biochar and can be converted into different three-dimensional functional nano materials. Biochar is known as Pb because of its higher carbon and hydrogen content, more oxygen-containing functional groups (e.g., O-H and C ═ O) 2+ 、Zn 2+ 、Hg 2+ And (3) a modifier for the water body and soil polluted by heavy metals. However, biochar has poor selectivity for heavy metal ions, so it needs to be modified to enhance the heavy metal adsorption capacity of the material by enhancing specific surface and chemical properties. Therefore, the CNF aerogel modified can effectively enhance the adsorption sites of the material, and is meaningful for researching and removing the sewage containing mercury ions.
Disclosure of Invention
The invention aims to: aiming at the problems, the invention provides a molybdenum disulfide/carbon nanofiber aerogel adsorbent with high active sites and a preparation method thereof, and the invention obtains the adsorbent with unique active sites by an improved methodW-MoS of specific molecular Structure 2 CNF, not only increasing MoS 2 The interlayer spacing of (2) also avoids MoS 2 The possibility of secondary pollution of the adsorbent is reduced; compared with other chelating agents, the water treatment agent has stronger chelation with metal ions and more adsorption sites, and has excellent treatment effect on the sewage containing mercury ions.
In order to achieve the purpose, the technical scheme adopted by the invention is as follows:
the preparation method of the high-activity-site molybdenum disulfide/carbon nanofiber aerogel adsorbent comprises the following steps:
(1) soaking and washing the cellulose acetate with deionized water, and then placing the cellulose acetate in a tubular furnace in a nitrogen protective atmosphere to heat to 400-plus-700 ℃, and preserving the heat for 150min at the temperature of 100-plus-150 min to obtain black carbon nanofiber aerogel;
(2) weighing soluble ammonium molybdate tetrahydrate and soluble thiourea according to the molar ratio of 1:10-1:50, adding deionized water with the solid-liquid ratio of 1g:8-15ml, carrying out ultrasonic treatment until the ammonium molybdate tetrahydrate and the soluble thiourea are completely dissolved, and stirring uniformly to obtain a mixed solution A;
(3) adding the mixed solution A and the carbon nanofiber aerogel into a polytetrafluoroethylene reaction kettle; the solid-to-liquid ratio of the carbon nanofiber aerogel to the deionized water added in the step (2) is 1g:700-1750 ml; reacting under hydrothermal conditions, wherein the reaction temperature is 175-190 ℃, the hydrothermal time is 10-24 hours, and performing solid-liquid separation on the obtained product to obtain a crude sample B;
(4) washing the crude sample B with deionized water, and drying in a freeze vacuum dryer to obtain the sample W-MoS of the high-activity-site molybdenum disulfide/carbon nanofiber 2 CNF aerogel adsorbent.
In the present invention, it is preferable that the temperature rise in the step (1) is performed at a rate of 5 ℃/min.
In the present invention, preferably, the temperature of the heat preservation in the step (1) is 500 ℃, and the heat preservation time is 120 min.
In the present invention, preferably, the molar ratio of ammonium molybdate tetrahydrate and soluble thiourea in step (2) is 1: 30.
in the present invention, it is preferable that the reaction temperature in the step (3) is 180 ℃.
In the present invention, preferably, the freeze vacuum drying machine in step (4) is used for drying, the freezing temperature is-45 ℃, the time is 48 hours, and the vacuum degree is less than 20 Pa.
The invention protects the molybdenum disulfide/carbon nanofiber aerogel adsorbent with high active sites prepared by the preparation method.
The invention also protects the application of the molybdenum disulfide/carbon nanofiber aerogel adsorbent with high active sites, which is prepared by the preparation method, in sewage treatment or the application of the molybdenum disulfide/carbon nanofiber aerogel adsorbent as a sewage treatment agent.
In summary, due to the adoption of the technical scheme, the invention has the beneficial effects that:
1. the invention takes carbon nanofiber aerogel as a carrier, and has W-MoS with a unique molecular structure through simple one-step hydrothermal reaction 2 CNF aerogel nano-adsorbent. The carbon nanofiber aerogel obtained by carbonizing the cellulose acetate is in a nanometer level, and has a larger specific surface area and a rich microporous structure compared with micron-sized natural fibers selected in previous work. The cellulose (coconut) of the bacillus aceticus has wide source and low cost. The carbon nanofiber aerogel is used as one of biochar, so that the cost can be effectively reduced, and the environment cannot be polluted. On this basis, through inlaying molybdenum disulfide nanosheet on porous graphitization charcoal surface, on the one hand use carbon nanofiber aerogel can realize that molybdenum disulfide nanosheet distributes more evenly as the carrier, avoids molybdenum disulfide nanosheet to the at utmost to appear piling up the phenomenon of reuniting, can improve the load factor to molybdenum disulfide to a certain extent greatly. On the other hand, the molybdenum disulfide nanosheets with widened interlayer spacing and increased defects can expose more sulfur-containing sites, mercury ions can be fully combined with the adsorbent, the effect of treating the sewage containing the mercury ions is very excellent, and the W-MoS prepared by the method disclosed by the invention 2 The adsorption capacity of the CNF aerogel on mercury ions in sewage reaches 1562mg/g, the removal rate is about 99 percent, and the CNF aerogel has higher adsorption capacity, better removal efficiency and excellent separation on mercury metal ions in sewageSub-selectivity, can be applied to the field of sewage treatment.
2. Under the best condition, the selective removal of mercury ions in the aqueous solution by other metal ions has no obvious influence, and the removal efficiency of the adsorbent on the mercury ions can still reach 99%. After the water body is purified according to the method provided by the invention, the adsorbent can be clamped out by using tweezers, and the separation of pollutants from the water body can be realized. And the adsorbent material can be recycled by soaking it in a 1M hydrochloric acid solution. In addition, the 2 times of purification-recovery-purification circulation does not disturb the order of the structure, the adsorption performance of the adsorption material per se has no sign of attenuation, and the adsorption material can be repeatedly used for further separating mercury ions in water.
3. The preparation method of the invention is convenient to operate, the raw materials are cheap and easy to obtain, and the industrial production and popularization and use are easy. The method has good application prospect in water environment pollution events, and particularly has extremely high efficiency in removing mercury ions.
Drawings
FIG. 1 shows the W-MoS high active site prepared in example 2 2 Powder diffraction (XRD) pattern of CNF aerogel.
FIG. 2 is the MoS prepared in example 4 2 Powder diffraction (XRD) pattern of CNF aerogel.
FIG. 3 is the MoS prepared in example 5 2 Powder diffraction (XRD) pattern of CNF aerogel.
FIG. 4 shows the W-MoS high active site prepared in example 2 2 Scanning Electron Microscope (SEM) image of CNF aerogel.
FIG. 5 shows the W-MoS high active site prepared in example 2 2 Transmission Electron Microscopy (TEM) image of/CNF aerogel.
FIG. 6 is the MoS prepared in example 4 2 Transmission Electron Microscopy (TEM) image of/CNF aerogel.
FIG. 7 is the MoS prepared in example 5 2 Transmission Electron Microscopy (TEM) image of/CNF aerogel.
FIG. 8 shows the W-MoS high active sites prepared in examples 1 to 3 2 CNF aerogel to Hg 2+ Adsorption kinetics curve of (1).
FIG. 9 shows the W-MoS high active sites prepared in examples 1 to 3 2 CNF aerogel to Hg 2+ Adsorption isotherm of (2).
FIG. 10 shows the W-MoS high active sites prepared in examples 1 to 3 2 /CNF aerogel can be used for treating Hg in interfering ion environment 2+ Ion selectivity of (1).
FIG. 11 shows the high active site W-MoS prepared in examples 1-3 2 The removal rate of CNF aerogel after twice recycling.
Detailed Description
In order to express the present invention more clearly, the present invention will be further illustrated by the following specific examples and comparative examples.
First, preparation example:
example 1
The preparation method of the high-activity-site molybdenum disulfide/carbon nanofiber aerogel adsorbent comprises the following steps:
(1) soaking and washing the cellulose acetate with deionized water for 3 times, and then placing the cellulose acetate in a tubular furnace in a nitrogen protective atmosphere to heat to 400 ℃ at a speed of 4 ℃/min, and preserving the heat for 150min to obtain black carbon nanofiber aerogel;
(2) weighing 1.24g of soluble ammonium molybdate tetrahydrate and 0.76g of soluble thiourea according to the molar ratio of 1:10, adding 16ml of deionized water, performing ultrasonic treatment until the ammonium molybdate tetrahydrate and the soluble thiourea are completely dissolved, and uniformly stirring to obtain a mixed solution A;
(3) adding the mixed solution A and the carbon nanofiber aerogel into a polytetrafluoroethylene reaction kettle; the solid-to-liquid ratio of the carbon nanofiber aerogel to the deionized water added in the step (2) is 1g to 700 ml; reacting under a hydrothermal condition, wherein the reaction temperature is 175 ℃, the hydrothermal time is 24 hours, and performing solid-liquid separation on the obtained product to obtain a crude sample B;
(4) washing the crude sample B with deionized water, and drying in a freeze vacuum drier at-45 deg.C for 48 hr with vacuum degree less than 20Pa to obtain the sample W-MoS of the high-activity-site molybdenum disulfide/carbon nanofiber 2 CNF aerogel adsorbent.
Example 2
The preparation method of the high-activity-site molybdenum disulfide/carbon nanofiber aerogel adsorbent comprises the following steps:
(1) soaking and washing the cellulose acetate with deionized water for several times, and then placing the cellulose acetate in a tubular furnace in a nitrogen protective atmosphere, heating to 500 ℃ at a speed of 5 ℃/min, and preserving heat for 120min to obtain black carbon nanofiber aerogel;
(2) weighing 1.24g of soluble ammonium molybdate tetrahydrate and 2.28g of soluble thiourea according to the molar ratio of 1:30, adding 35ml of deionized water, performing ultrasonic treatment until the ammonium molybdate tetrahydrate and the soluble thiourea are completely dissolved, and uniformly stirring to obtain a mixed solution A;
(3) adding the mixed solution A and the carbon nanofiber aerogel into a polytetrafluoroethylene reaction kettle; the solid-to-liquid ratio of the carbon nanofiber aerogel to the deionized water added in the step (2) is 1g to 875 ml; reacting under a hydrothermal condition, wherein the reaction temperature is 180 ℃, the hydrothermal time is 24 hours, and performing solid-liquid separation on the obtained product to obtain a crude sample B;
(4) washing the crude sample B with deionized water, and drying in a freeze vacuum drier at-45 deg.C for 48 hr with vacuum degree less than 20Pa to obtain the sample W-MoS of the high-activity-site molybdenum disulfide/carbon nanofiber 2 CNF aerogel adsorbent.
Example 3
The preparation method of the high-activity-site molybdenum disulfide/carbon nanofiber aerogel adsorbent comprises the following steps:
(1) soaking and washing the cellulose acetate with deionized water for several times, and then placing the cellulose acetate in a tubular furnace in a nitrogen protective atmosphere, heating to 700 ℃ at the speed of 6 ℃/min, and preserving heat for 100min to obtain black carbon nanofiber aerogel;
(2) weighing 1.24g of soluble ammonium molybdate tetrahydrate and 2.8g of soluble thiourea according to the molar ratio of 1:50, adding 60.6ml of deionized water, performing ultrasonic treatment until the solution is completely dissolved, and uniformly stirring to obtain a mixed solution A;
(3) adding the mixed solution A and the carbon nanofiber aerogel into a polytetrafluoroethylene reaction kettle; the solid-to-liquid ratio of the carbon nanofiber aerogel to the deionized water added in the step (2) is 1g to 1750 ml; reacting under a hydrothermal condition, wherein the reaction temperature is 190 ℃, the hydrothermal time is 10 hours, and performing solid-liquid separation on the obtained product to obtain a crude sample B;
(4) washing the crude sample B with deionized water, and drying in a freeze vacuum drier at-45 deg.C for 48 hr with vacuum degree less than 20Pa to obtain the sample W-MoS of the high-activity-site molybdenum disulfide/carbon nanofiber 2 CNF aerogel adsorbent.
Example 4
The preparation method of the molybdenum disulfide/carbon nanofiber aerogel adsorbent comprises the following steps:
(1) soaking and washing the cellulose acetate with deionized water for several times, and then placing the cellulose acetate in a tubular furnace in a nitrogen protective atmosphere, heating to 500 ℃ at a speed of 5 ℃/min, and preserving heat for 120min to obtain black carbon nanofiber aerogel;
(2) weighing 1.24g of soluble ammonium molybdate tetrahydrate and 2.28g of soluble thiourea according to the molar ratio of 1:30, adding 35ml of deionized water, performing ultrasonic treatment until the ammonium molybdate tetrahydrate and the soluble thiourea are completely dissolved, and uniformly stirring to obtain a mixed solution A;
(3) adding the mixed solution A and the carbon nanofiber aerogel into a polytetrafluoroethylene reaction kettle; the solid-to-liquid ratio of the carbon nanofiber aerogel to the deionized water added in the step (2) is 1g to 875 ml; reacting under a hydrothermal condition, wherein the reaction temperature is 170 ℃, the hydrothermal time is 24 hours, and performing solid-liquid separation on the obtained product to obtain a crude sample B;
(4) washing the crude sample B with deionized water, and drying in a freeze vacuum drier at-45 deg.C for 48 hr with vacuum degree less than 20Pa to obtain the sample MoS 2 CNF aerogel adsorbent.
Example 5
The preparation method of the molybdenum disulfide/carbon nanofiber aerogel adsorbent comprises the following steps:
(1) soaking and washing the cellulose acetate with deionized water for several times, and then placing the cellulose acetate in a tubular furnace in a nitrogen protective atmosphere, heating to 500 ℃ at a speed of 5 ℃/min, and preserving heat for 120min to obtain black carbon nanofiber aerogel;
(2) weighing 1.24g of soluble ammonium molybdate tetrahydrate and 2.28g of soluble thiourea according to the molar ratio of 1:30, adding 35ml of deionized water, performing ultrasonic treatment until the ammonium molybdate tetrahydrate and the soluble thiourea are completely dissolved, and uniformly stirring to obtain a mixed solution A;
(3) adding the mixed solution A and the carbon nanofiber aerogel into a polytetrafluoroethylene reaction kettle; the solid-to-liquid ratio of the carbon nanofiber aerogel to the deionized water added in the step (2) is 1g to 875 ml; reacting under a hydrothermal condition, wherein the reaction temperature is 195 ℃, the hydrothermal time is 24 hours, and performing solid-liquid separation on the obtained product to obtain a crude sample B;
(4) washing the crude sample B with deionized water, and drying in a freeze vacuum drier at-45 deg.C for 48 hr with vacuum degree less than 20Pa to obtain the sample MoS 2 CNF aerogel adsorbent.
Second, product confirmation
1. The W-MoS prepared in examples 1-3 was used 2 The CNF aerogel is subjected to X-ray powder diffraction analysis, and the W-MoS can be seen from the X-ray powder diffraction structure characterization of the material 2 the/CNF aerogel has obvious characteristic diffraction peaks in a low-angle area less than 10 degrees, corresponds to (002) diffraction peaks on a standard card (PDF #37-1492) of molybdenum disulfide, and obtains MoS in the composite material through calculation 2 Has a layer spacing of
Figure BDA0003341107940000071
The layer spacing of the raw molybdenum disulfide material without broadening is
Figure BDA0003341107940000072
Illustrating the broadening of the interlayer spacing of molybdenum disulfide in the composite, wherein the W-MoS obtained in example 2 2 The powder diffraction (XRD) pattern of the/CNF aerogel is shown in figure 1.
For the W-MoS obtained in examples 4 and 5 2 The CNF aerogel is subjected to X-ray powder diffraction analysis, and the W-MoS can be seen from the X-ray powder diffraction structure characterization of the material 2 CNF aerogels at low angles of less than 10 DEGThe degree zone has obvious characteristic diffraction peak corresponding to (002) diffraction peak on standard card (PDF #37-1492) of molybdenum disulfide, and MoS in the composite material is obtained by calculation 2 Has a layer spacing of
Figure BDA0003341107940000073
And
Figure BDA0003341107940000074
indicating that the interlayer spacing of molybdenum disulfide in the composite did not expand to a sufficiently wide distance, where the MoS obtained in examples 4 and 5 2 The powder diffraction (XRD) patterns of the/CNF aerogel are shown in figures 2 and 3.
2. For the W-MoS prepared in examples 1-3 2 SEM scanning electron microscope analysis of/CNF aerogel shows that the composite material maintains the net-shaped three-dimensional structure of the carbon nanofiber aerogel and the surface of the fiber is coated with MoS 2 The molybdenum disulfide has a nano-scale sheet structure and has a certain degree of curling, which is the subsequent Hg 2+ Provides a larger specific surface area and more adsorption sites. Wherein, the W-MoS obtained in example 2 2 The Scanning Electron Microscope (SEM) image of the/CNF aerogel is shown in FIG. 4.
3. For the W-MoS prepared in examples 1-3 2 TEM transmission electron microscope analysis of the/CNF aerogel shows that the spacing between adjacent lattice fringes is about
Figure BDA0003341107940000075
Corresponding to MoS 2 The spacing of (002) crystal planes of (A) is consistent with XRD data, and W-MoS is further confirmed 2 MoS in CNF aerogel 2 The inter-layer spacing is widened. HRTEM image display MoS 2 The presence of a large number of crystal defects in the nanosheets revealed MoS 2 Defect-rich features and relatively disordered arrangement of atoms along the substrate plane due to large numbers of dislocations and twists. Selected Area Electron Diffraction (SAED) maps further confirm this feature. These defects may lead to the formation of cracks and cavities on the basal plane, which may act as Hg 2+ Additional diffusion channels. Wherein, the W-MoS obtained in example 2 2 A Transmission Electron Microscope (TEM) image of the/CNF aerogel is shown in FIG. 5.
MoS obtained in examples 4 and 5 2 TEM transmission electron microscope analysis of the/CNF aerogel shows that the spacing between adjacent lattice fringes is about
Figure BDA0003341107940000076
And
Figure BDA0003341107940000077
corresponding to MoS 2 The spacing of (002) crystal planes is consistent with XRD data, and MoS is further confirmed 2 MoS in CNF aerogel 2 Interlayer spacing versus commercial MoS 2 Widening but slightly smaller interlayer spacing compared to example 2. In which the MoS obtained in examples 4 and 5 2 Transmission Electron Microscopy (TEM) images of the/CNF aerogels are shown in FIGS. 6 and 7.
Examples 4 and 5 differ from example 2 in the temperature of the hydrothermal reaction, which shows that the control of the temperature in the present invention has a large influence on the morphology of the product and ultimately on the activity of the material, and examples 4 and 5 fail to obtain W-MoS having a greatly improved morphology 2 /CNF aerogel.
Thirdly, performance test:
1. 50mg of the adsorbents prepared in the above examples 1 to 3 were weighed, added to 100mL of a mercury ion-containing solution with a concentration of 10ppm, shaken at a constant temperature of 25 ℃, sampled at different times within 0 to 24 hours, and the obtained samples were subjected to ICP-MS measurement of the concentration of mercury ions. Drawing W-MoS 2 The adsorption kinetics curve of the/CNF aerogel is shown in FIG. 8, and when the adsorption equilibrium is reached, the mercury ion removal rate of the prepared adsorbent is 99%.
2. 50mg of the adsorbent prepared in the above examples 1 to 3 was weighed and placed in 100mL of a mercury ion-containing solution with a concentration of 1 to 500ppm, and the solution was shaken at a constant temperature of 25 ℃ for 24 hours, and the concentration of mercury ions in the solution after reaction equilibrium was measured by ICP-MS. Drawing W-MoS 2 The adsorption isotherm of the/CNF aerogel is shown in FIG. 9, and after the reaction is balanced, the maximum adsorption capacity of the adsorbent reaches 1562 mg/g. Higher than the literature (j. colloid. inter. sci.2019,551,251-260.) reported Fe 3 O 4 @MoS 2 The maximum adsorption capacity for adsorbing mercury ions is 526 mg/g. Proves that the W-MoS of the invention 2 The CNF aerogel has better mercury ion adsorption effect.
3. The anti-interference ion capacity of the adsorption material synthesized by the invention is measured. 50mg of the adsorbent prepared in examples 1-3 above was loaded in 100mL of a solution of zinc (Zn) 2+ ) Manganese (Mn) 2+ ) Nickel (Ni) 2+ ) Cadmium (Cd) 2+ ) Cobalt (Co) 2+ ) Chromium (Cr) 3+ ) Copper (Cu) 2+ ) Lead (Pb) 2+ ) The removal rate and K of the adsorbent were measured under the interference of various ions (the above ion concentrations were all 10ppm) d The value is obtained. For the W-MoS synthesized in the invention 2 The anti-interference ion capacity of the CNF aerogel is measured. As a result, as shown in FIG. 10, the distribution coefficient of the material to mercury ions can still reach 10 5 mLg -1 And the removal rate reaches 99 percent.
4. Respectively weighing 50mg of the adsorbent prepared in the above examples 1-3, adding the adsorbent into 100mL of mercury ion-containing solution with the concentration of 10ppm, shaking at a constant temperature of 25 ℃, and measuring the concentration of mercury ions by using ICP-MS after 20 min; the adsorbent was taken out and immersed in a 1M hydrochloric acid solution to be recycled. Taking back the recycled adsorbing material, cleaning, adding into 100mL of mercury ion-containing solution with the concentration of 10ppm, shaking at constant temperature of 25 ℃, and measuring the concentration of mercury ions by using ICP-MS after 20 min; the mercury ion removal rate is calculated each time, as shown in fig. 11, it can be seen that the mercury ion removal rate of the recycled adsorbent is still 99%, and the recycled adsorbent has better recyclability.
The above description is intended to describe in detail the preferred embodiments of the present invention, but the embodiments are not intended to limit the scope of the claims of the present invention, and all equivalent changes and modifications made within the technical spirit of the present invention should fall within the scope of the claims of the present invention.

Claims (8)

1. The preparation method of the high-activity-site molybdenum disulfide/carbon nanofiber aerogel adsorbent is characterized by comprising the following steps of:
(1) soaking and washing the cellulose acetate with deionized water, and then placing the cellulose acetate in a tubular furnace in a nitrogen protective atmosphere to heat to 400-plus-700 ℃, and preserving the heat for 150min at the temperature of 100-plus-150 min to obtain black carbon nanofiber aerogel;
(2) weighing soluble ammonium molybdate tetrahydrate and soluble thiourea according to the molar ratio of 1:10-1:50, adding deionized water with the solid-liquid ratio of 1g:8-15ml, carrying out ultrasonic treatment until the ammonium molybdate tetrahydrate and the soluble thiourea are completely dissolved, and stirring uniformly to obtain a mixed solution A;
(3) adding the mixed solution A and the carbon nanofiber aerogel into a polytetrafluoroethylene reaction kettle; the solid-to-liquid ratio of the carbon nanofiber aerogel to the deionized water added in the step (2) is 1g: 700-; reacting under hydrothermal conditions, wherein the reaction temperature is 175-190 ℃, the hydrothermal time is 10-24 hours, and performing solid-liquid separation on the obtained product to obtain a crude sample B;
(4) washing the crude sample B with deionized water, and drying in a freeze vacuum drier to obtain the sample W-MoS of the high-activity-site molybdenum disulfide/carbon nanofiber 2 CNF aerogel adsorbent.
2. The method of claim 1, wherein: the temperature rise in the step (1) is carried out at a speed of 5 ℃/min.
3. The method of claim 1, wherein: the temperature for heat preservation in the step (1) is 500 ℃, and the heat preservation time is 120 min.
4. The method of claim 1, wherein: the mol ratio of the ammonium molybdate tetrahydrate to the soluble thiourea in the step (2) is 1: 30.
5. the method of claim 1, wherein: the reaction temperature in the step (3) is 180 ℃.
6. The method of claim 1, wherein: and (4) drying by using the freezing vacuum dryer in the step (4), wherein the freezing temperature is-45 ℃, the time is 48 hours, and the vacuum degree is less than 20 Pa.
7. The high-activity-site molybdenum disulfide/carbon nanofiber aerogel adsorbent prepared according to the preparation method of any one of claims 1 to 6.
8. The application of the high-activity-site molybdenum disulfide/carbon nanofiber aerogel adsorbent prepared by the preparation method according to any one of claims 1 to 6 in sewage treatment or as a sewage treatment agent.
CN202111399350.6A 2021-11-05 2021-11-05 High-activity-site molybdenum disulfide/carbon nanofiber aerogel adsorbent and preparation method thereof Pending CN114950353A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202111399350.6A CN114950353A (en) 2021-11-05 2021-11-05 High-activity-site molybdenum disulfide/carbon nanofiber aerogel adsorbent and preparation method thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202111399350.6A CN114950353A (en) 2021-11-05 2021-11-05 High-activity-site molybdenum disulfide/carbon nanofiber aerogel adsorbent and preparation method thereof

Publications (1)

Publication Number Publication Date
CN114950353A true CN114950353A (en) 2022-08-30

Family

ID=82974793

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202111399350.6A Pending CN114950353A (en) 2021-11-05 2021-11-05 High-activity-site molybdenum disulfide/carbon nanofiber aerogel adsorbent and preparation method thereof

Country Status (1)

Country Link
CN (1) CN114950353A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN115608324A (en) * 2022-09-22 2023-01-17 宁德师范学院 Organic-inorganic hybrid mesoporous mercury ion adsorption material and preparation method thereof

Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101480605A (en) * 2009-01-05 2009-07-15 浙江工业大学 Novel activated carbon fiber adsorbing substance as well as preparation method and use thereof
CN102794157A (en) * 2011-05-25 2012-11-28 周鑫 Composite medium capable of adsorbing heavy metals
CN103011864A (en) * 2012-12-21 2013-04-03 中国科学技术大学 Carbon nanofiber aerogel as well as preparation method and application thereof
CN105056885A (en) * 2015-07-29 2015-11-18 江琴 Active carbon absorbent for removing mercury in flue gas
CN105126876A (en) * 2015-09-07 2015-12-09 复旦大学 Flowerlike carbon-loaded MoS<2> nano-particle composite and preparation method thereof
CN105617956A (en) * 2016-01-28 2016-06-01 复旦大学 Molybdenum disulfide nanosheet/polyimide based composite aerogel and preparation method thereof
CN106391058A (en) * 2016-08-22 2017-02-15 河南师范大学 Method for preparing monolayer 1T phase molybdenum disulfide/micro-nano carbon composite material
CN108137343A (en) * 2015-10-08 2018-06-08 曼彻斯特大学 Aeroge
CN109289805A (en) * 2018-10-12 2019-02-01 南京林业大学 A kind of method nano-cellulose composite aerogel adsorbent preparation and its adsorb heavy metal ion
CN110038492A (en) * 2019-04-29 2019-07-23 福州大学 A kind of regeneration cotton fiber preparation MoS2The method and its application of@C aeroge

Patent Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101480605A (en) * 2009-01-05 2009-07-15 浙江工业大学 Novel activated carbon fiber adsorbing substance as well as preparation method and use thereof
CN102794157A (en) * 2011-05-25 2012-11-28 周鑫 Composite medium capable of adsorbing heavy metals
CN103011864A (en) * 2012-12-21 2013-04-03 中国科学技术大学 Carbon nanofiber aerogel as well as preparation method and application thereof
CN105056885A (en) * 2015-07-29 2015-11-18 江琴 Active carbon absorbent for removing mercury in flue gas
CN105126876A (en) * 2015-09-07 2015-12-09 复旦大学 Flowerlike carbon-loaded MoS<2> nano-particle composite and preparation method thereof
CN108137343A (en) * 2015-10-08 2018-06-08 曼彻斯特大学 Aeroge
CN105617956A (en) * 2016-01-28 2016-06-01 复旦大学 Molybdenum disulfide nanosheet/polyimide based composite aerogel and preparation method thereof
CN106391058A (en) * 2016-08-22 2017-02-15 河南师范大学 Method for preparing monolayer 1T phase molybdenum disulfide/micro-nano carbon composite material
CN109289805A (en) * 2018-10-12 2019-02-01 南京林业大学 A kind of method nano-cellulose composite aerogel adsorbent preparation and its adsorb heavy metal ion
CN110038492A (en) * 2019-04-29 2019-07-23 福州大学 A kind of regeneration cotton fiber preparation MoS2The method and its application of@C aeroge

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
JIAN-GAN WANG ET AL.: "Uniform growth of MoS2 nanosheets on carbon nanofibers with enhanced electrochemical utilization for Li-ion batteries", ELECTROCHIMICA ACTA, vol. 231, pages 396 - 402, XP085134127, DOI: 10.1016/j.electacta.2017.01.108 *
艾可龙 等: "硫化钼的另一面:高效的汞离子吸附剂", 中国化学会第30届学术年会摘要集-第二十六分会:环境化学, pages 302 *

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN115608324A (en) * 2022-09-22 2023-01-17 宁德师范学院 Organic-inorganic hybrid mesoporous mercury ion adsorption material and preparation method thereof

Similar Documents

Publication Publication Date Title
Yang et al. Corn straw-derived biochar impregnated with α-FeOOH nanorods for highly effective copper removal
Yang et al. Assembling biochar with various layered double hydroxides for enhancement of phosphorus recovery
Zuo et al. Enhanced removal of Cd (II) from aqueous solution using CaCO 3 nanoparticle modified sewage sludge biochar
Fu et al. Fabrication of α-FeOOH decorated graphene oxide-carbon nanotubes aerogel and its application in adsorption of arsenic species
Luo et al. Amino siloxane oligomer-linked graphene oxide as an efficient adsorbent for removal of Pb (II) from wastewater
Dai et al. Engineered hydrochar composites for phosphorus removal/recovery: lanthanum doped hydrochar prepared by hydrothermal carbonization of lanthanum pretreated rice straw
Shen et al. Alginate modified graphitic carbon nitride composite hydrogels for efficient removal of Pb (II), Ni (II) and Cu (II) from water
Du et al. MnO2 nanowires in situ grown on diatomite: Highly efficient absorbents for the removal of Cr (VI) and As (V)
JP7197626B2 (en) Method for producing iron-carbon composite material
Mario et al. Molybdenum disulfide/montmorillonite composite as a highly efficient adsorbent for mercury removal from wastewater
Tian et al. A novel GO/PNIPAm hybrid with two functional domains can simultaneously effectively adsorb and recover valuable organic and inorganic resources
Zhang et al. Analog synthesis of artificial humic substances for efficient removal of mercury
Li et al. Uniform surface modification of diatomaceous earth with amorphous manganese oxide and its adsorption characteristics for lead ions
Liu et al. An antibacterial and antifouling amidoxime-functionalized graphene oxide aerogel for selective uranium adsorption in Salt Lake water
CN102275998A (en) Preparation method of magnetic Fe3O4 nanoparticles and application thereof in adsorption and separation of heavy metal ions
Sharma et al. Fe–Al based nanocomposite reinforced hydrothermal carbon: Efficient and robust absorbent for anionic dyes
Pei et al. Interfacial growth of nitrogen-doped carbon with multi-functional groups on the MoS2 skeleton for efficient Pb (II) removal
Wang et al. Preparation, kinetics, and adsorption mechanism study of microcrystalline cellulose-modified bone char as an efficient Pb (II) adsorbent
Wei et al. Synthesis of 3D lotus biochar/reduced graphene oxide aerogel as a green adsorbent for Cr (VI)
Ali et al. Magnetically active nanocomposite aerogels: preparation, characterization and application for water treatment
Zhou et al. Adsorption properties of a novel 3D graphene/MgO composite for heavy metal ions
Zhang et al. MoxPy nanoparticles supported on mesh structural carbon from biomass for rapid selective dyes adsorption
CN114950353A (en) High-activity-site molybdenum disulfide/carbon nanofiber aerogel adsorbent and preparation method thereof
CN112897496B (en) Graphene-like biochar for heavy metal removal and preparation method thereof
Liu et al. Facile method of synthesizing multilayer graphene capsuled sulfur nanoparticles for water treatment

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