CN112675810B - Amorphous high-efficiency phosphorus removal adsorption material, preparation method and water treatment application thereof - Google Patents

Amorphous high-efficiency phosphorus removal adsorption material, preparation method and water treatment application thereof Download PDF

Info

Publication number
CN112675810B
CN112675810B CN202011401625.0A CN202011401625A CN112675810B CN 112675810 B CN112675810 B CN 112675810B CN 202011401625 A CN202011401625 A CN 202011401625A CN 112675810 B CN112675810 B CN 112675810B
Authority
CN
China
Prior art keywords
cerium
preparation
amorphous
phosphorus removal
stirring
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.)
Active
Application number
CN202011401625.0A
Other languages
Chinese (zh)
Other versions
CN112675810A (en
Inventor
王威
单苏洁
张涛
崔福义
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.)
Harbin Institute of Technology
Original Assignee
Harbin Institute of Technology
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 Harbin Institute of Technology filed Critical Harbin Institute of Technology
Priority to CN202011401625.0A priority Critical patent/CN112675810B/en
Publication of CN112675810A publication Critical patent/CN112675810A/en
Application granted granted Critical
Publication of CN112675810B publication Critical patent/CN112675810B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Abstract

An amorphous high-efficiency dephosphorization adsorption material and a preparation method and application thereof, belonging to the technical field of water treatment material preparation. The invention mainly aims at the problems of limited removal amount, complex preparation and the like of the existing dephosphorization adsorbing material, and aims to construct the amorphous efficient dephosphorization adsorbing material which has high saturated adsorption capacity, stable pH and is not influenced by water quality by using a one-pot reaction and taking a natural clay mineral material as a substrate and co-loading amorphous cerium carbonate and ferrous carbonate nano particles on the surface of the structure. The preparation method mainly comprises the following steps: adding natural clay mineral material, cerium salt, ferric salt and urea into water, stirring for 0.5-10 h, and adding a reducing agent; stirring for 0.3-2 hr to mix homogeneously, further stirring at 60-100 deg.c for 2-24 hr, solid-liquid separating, washing several times and drying in 40-80 deg.c oven. The preparation method has the advantages of simple preparation process, convenient operation, easily obtained raw materials and better application prospect.

Description

Amorphous high-efficiency phosphorus removal adsorption material, preparation method thereof and water treatment application
Technical Field
The invention belongs to the technical field of water treatment material preparation, and particularly relates to an efficient phosphorus removal adsorption material of amorphous cerium-iron co-modified natural clay minerals, and a preparation method and application thereof.
Background
Eutrophication of water bodies is known to cause algal mass propagation, oxygen depletion in the water, death of biological organisms and disruption of aquatic ecological balance. Among them, excessive nitrogen and phosphorus are the main causes of water eutrophication. However, research generally considers that the over-standard phosphorus content is a decisive factor for causing the eutrophication phenomenon of the water body, so that the phosphorus removal of the water body is very important for controlling the eutrophication. The adsorption method for removing phosphorus has the advantages of simple operation, high efficiency and the like, and is concerned in a plurality of phosphorus removal methods.
Cerium is the element with the highest abundance in rare earth elements, has a unique 4f electronic structure, can form a complex with a Lewis base substance functional group, and has a special adsorption effect on phosphate ions. Because nanoparticles are easy to agglomerate, a large number of active sites are difficult to utilize, so in order to realize the maximum utilization of cerium-based active adsorption sites, at present, cerium nanoparticles are mainly loaded on various carriers to realize the dispersion of cerium nanomaterials and strengthen the contact and adsorption of the cerium nanoparticles on phosphate radicals. In general, the characteristics of the support material can affect the loading of the nanoparticles, which in turn affects the adsorption of contaminants by the composite adsorbent material. At present, the documents report that orange peel, chitosan, lignin or biochar are used as carriers, and loaded cerium ions, cerium oxide or cerium hydroxide are used as phosphorus removal adsorption materials. However, most of them have the disadvantages of complex preparation, low adsorption capacity, poor removal effect in low-concentration phosphorus environment, poor pH stability or easy interference of coexisting ions, etc., which severely limits their application in actual phosphorus removal from water.
Some natural clay mineral materials, such as sepiolite, attapulgite, halloysite, bentonite, diatomite, kaolin and the like, are abundant in reserves and low in price, have high cation exchange performance and large specific surface area, and are often used as high-quality catalyst carriers and adsorption materials. In water environment, the natural clay mineral material has very limited removal amount of phosphate because the surface of the natural clay mineral material has higher net negative charge, so that the natural clay mineral material is difficult to combine with phosphate anions with negative charges.
Disclosure of Invention
The invention aims to solve the problems of limited removal amount, complex preparation, high preparation cost, poor pH stability and the like of the existing dephosphorization adsorbing material, and provides an amorphous cerium-iron co-modified natural clay mineral efficient dephosphorization adsorbing material, and a preparation method and application thereof. Because the loaded cerium-iron nano particles are in an amorphous structure, the loaded cerium-iron nano particles have more defect sites and larger specific surface area, and can provide a large number of active sites. The adsorbing material prepared by the method has excellent phosphorus removal performance, simple process steps, used equipment and specific implementation, environmental friendliness, low price of raw materials, easiness in obtaining and good application prospect.
In order to achieve the purpose, the technical scheme adopted by the invention is as follows:
the phosphorus removal adsorbing material is formed by compounding amorphous cerium carbonate and ferrous carbonate nanoparticles and a natural clay mineral material, wherein the amorphous cerium carbonate and ferrous carbonate nanoparticles are attached to the structural surface of the natural clay mineral material.
A preparation method of the amorphous cerium-iron co-modified natural clay mineral high-efficiency dephosphorization adsorbing material comprises the following steps: adding untreated natural clay mineral material, cerium salt, ferric salt and urea into water, stirring for 0.5-10 h, and adding a reducing agent; and then, continuously stirring for 0.3 to 2 hours to uniformly mix, stirring for reaction at the temperature of 60 to 100 ℃ for 2 to 24 hours, carrying out solid-liquid separation on the product after the reaction is finished, cleaning, and drying at the temperature of 40 to 80 ℃ to obtain the efficient dephosphorization adsorbing material with the amorphous cerium-iron nano particles as the functional components.
The application of the amorphous cerium-iron co-modified natural clay mineral high-efficiency dephosphorization adsorbing material prepared in the way in removing phosphorus in various water bodies.
Compared with the prior art, the invention has the beneficial effects that:
(1) The preparation method has the advantages of simple preparation process, convenient operation, easily obtained raw materials and better application prospect;
(2) The cerium-iron co-modified natural clay mineral efficient phosphorus removal adsorption material prepared by the invention has a large specific surface area, amorphous cerium-iron nano particles are uniformly distributed and have small sizes, and the surface has many defects, so that the adsorption is facilitated;
(3) The amorphous cerium-iron co-modified natural clay mineral efficient phosphorus removal adsorption material prepared by the invention has the advantages of excellent phosphorus removal effect, stronger selectivity, higher adsorption capacity, higher adsorption rate, wide pH application range and better removal effect on low-concentration phosphorus.
(4) The invention takes untreated natural clay mineral material as a carrier, and the amorphous cerium-iron nano particles are loaded on the carrier together, thereby not only realizing the dispersion of the cerium nano particles, reasonably utilizing cerium active sites and reducing the dosage of cerium element, but also improving the defect of phosphorus removal performance of the original natural clay mineral material. The co-doping of the cheap iron element can further reduce the dosage of cerium in the composite adsorbing material and reduce the cost of the cerium-iron co-modified natural clay mineral efficient dephosphorization adsorbing material.
Drawings
FIG. 1 is XRD patterns of raw sepiolite, the amorphous high-efficiency phosphorus removal adsorption material obtained in example 2 and example 3;
FIG. 2 is an SEM image of the efficient dephosphorization adsorbent material of amorphous cerium-iron co-modified sepiolite obtained in example 3;
FIG. 3 is a FTIR diagram of efficient dephosphorization adsorbent material of raw sepiolite and amorphous cerium-iron co-modified sepiolite obtained in example 3;
FIG. 4 is a graph showing the kinetics of phosphorus adsorption of the phosphorus removal adsorbent obtained in example 3;
FIG. 5 is a graph showing isothermal adsorption for removing phosphorus from the phosphorus removal adsorbent obtained in example 3;
FIG. 6 is a graph showing the phosphorus removal effect of the phosphorus removal adsorbent obtained in example 3 at different pH values;
FIG. 7 is a graph showing the phosphorus removal effect of the phosphorus removal adsorbent obtained in example 3 under different coexisting ions;
Detailed Description
The technical solutions of the present invention are further described below by the drawings and examples, but the present invention is not limited thereto, and any modifications or equivalent substitutions may be made to the technical solutions of the present invention without departing from the spirit and scope of the technical solutions of the present invention.
The natural clay mineral material, the cerium salt, the ferric salt, the urea and the ascorbic acid solution are uniformly mixed according to a certain proportion, and the amorphous cerium carbonate and ferrous carbonate nano particle co-loaded natural clay mineral composite adsorbing material is successfully prepared through a simple one-pot reaction. The adsorbing material reserves the special framework structure of a natural clay mineral material, realizes the uniform dispersion of amorphous cerium carbonate and ferrous carbonate nanoparticles, greatly improves the phosphorus removal performance of the original natural clay mineral material, and has the saturated adsorption capacity of 50-73.68 mg-P/g for phosphate anions. Meanwhile, the preparation method has the advantages of low energy consumption, simple operation, no special equipment, good reproducibility and the like, and has good application prospect.
The first embodiment is as follows: the embodiment describes an amorphous cerium-iron co-modified natural clay mineral efficient dephosphorization adsorbing material, which is formed by compounding amorphous cerium carbonate and ferrous carbonate nanoparticles with a natural clay mineral material, wherein the amorphous cerium carbonate and ferrous carbonate nanoparticles are attached to the structural surface of the natural clay mineral material and can selectively adsorb phosphate in water, so that efficient removal of phosphorus in water is realized.
The second embodiment is as follows: in a specific embodiment, the amorphous cerium-iron co-modified natural clay mineral high-efficiency phosphorus removal adsorption material is prepared from one or more of calcium-rich sepiolite, magnesium-rich sepiolite, halloysite, attapulgite, bentonite, diatomite and kaolin, and is preferably magnesium-rich sepiolite.
The third concrete implementation mode: a preparation method of the amorphous cerium-iron co-modified natural clay mineral high-efficiency dephosphorization adsorbing material, which is described in the first embodiment or the second embodiment, the method comprises the following steps: adding untreated natural clay mineral material, cerium salt, ferric salt and urea into water, stirring for 0.5 to 10 hours, and adding a reducing agent; and then, continuously stirring for 0.3 to 2 hours to uniformly mix the cerium-iron-based nano particles, stirring for reaction at the temperature of between 60 and 100 ℃ for 2 to 24 hours, carrying out solid-liquid separation on a product after the reaction is finished, cleaning, and drying at the temperature of between 40 and 80 ℃ to obtain the efficient dephosphorization adsorbing material with the functional component of the amorphous cerium-iron nano particles. The material obtained by the invention can effectively remove phosphorus with different concentrations in raw water, tail water and various surface waters of a sewage treatment plant, and has the following unique characteristics: (1) The pH application range is wide, and the pH-sensitive adhesive can be effectively applied under the pH value of 3-10; (2) The specific adsorption capacity of phosphate radical is strong, and the saturated adsorption capacity of phosphorus can reach 73.68 mg-P/g; and (3) faster phosphorus adsorption removal rate.
The fourth concrete implementation mode is as follows: in the preparation method of the efficient dephosphorization adsorbent material for amorphous cerium-iron co-modified natural clay mineral according to the third embodiment, the cerium salt is one or more of cerium chloride, cerium nitrate and a hydrate thereof, preferably cerium nitrate hexahydrate; the iron salt is one or more of ferric chloride, ferric nitrate, ferric sulfate and hydrate thereof, and ferric chloride hexahydrate is preferred.
The fifth concrete implementation mode is as follows: in the preparation method of the amorphous cerium-iron co-modified natural clay mineral high-efficiency phosphorus removal adsorption material according to the third embodiment, the molar ratio of the cerium salt to the iron salt is 3:1 to 6, preferably 1:1; the mass ratio of the cerium salt to the natural clay mineral material is 0.03 to 1 in terms of cerium ion content: 1, preferably 0.15:1; the molar ratio of urea to the sum of the total amount of cerium salt and iron salt is 5-50: 1, preferably 25:1.
the sixth specific implementation mode is as follows: in the third specific embodiment, the stirring mode is magnetic stirring or mechanical stirring, and the stirring speed is 400 to 1000 r/min.
The seventh concrete implementation mode: in the preparation method of the amorphous cerium-iron co-modified natural clay mineral high-efficiency phosphorus removal adsorbing material, the reducing agent is one or more of ascorbic acid, hydrazine hydrate and citric acid, and the molar usage ratio of the reducing agent to the iron salt is 1 to 5.
The specific implementation mode is eight: in the preparation method of the amorphous cerium-iron co-modified natural clay mineral high-efficiency phosphorus removal adsorbing material, the water bath temperature is 60 to 100 ℃, preferably 85 ℃, and the reaction time is 2 to 24 hours, preferably 4 hours.
The specific implementation method nine: in the preparation method of the amorphous cerium-iron co-modified natural clay mineral high-efficiency dephosphorization adsorbing material according to the third specific embodiment, the solid-liquid separation is one of centrifugal separation, gravity settling and filtration separation.
The detailed implementation mode is ten: an application of the adsorption material obtained by the preparation method of the amorphous cerium-iron co-modified natural clay mineral high-efficiency phosphorus removal adsorption material in removal of phosphorus in various water bodies according to any one of the third to ninth embodiments.
Example 1:
dissolving 2.0 g of 400-mesh attapulgite, 1.31 g of cerous nitrate hexahydrate, 0.82 g of ferric chloride hexahydrate and 9 g of urea in 100 mL of water, and stirring for 5 hours on a magnetic stirrer; after the solution is uniformly mixed, adding 1 g of ascorbic acid into the solution, and continuously stirring the solution for 1 hour; then heating and stirring the mixture at 85 ℃ for reaction for 4 hours, and controlling the rotating speed to be 500 r/min. After the reaction is finished, the product is subjected to solid-liquid separation and washing for a plurality of times, and is dried for 12 hours at 50 ℃ to obtain the modified attapulgite high-efficiency dephosphorization adsorbing material with the functional component of amorphous cerium-iron nano particles.
Example 2:
dissolving 4 g of sepiolite, 1.31 g of cerous nitrate hexahydrate, 0.82 g of ferric chloride hexahydrate and 9 g of urea in 100 mL of water, and stirring for 1 hour on a magnetic stirrer; after the solution is uniformly mixed, 1 g of ascorbic acid is added into the solution, and the solution is continuously stirred for 0.5 h; then heating and stirring the mixture at 85 ℃ for reaction for 4 hours, and controlling the rotating speed to be 500 r/min. After the reaction is finished, the product is subjected to solid-liquid separation and cleaning for a plurality of times, and is dried for 12 hours at 50 ℃ to obtain the modified sepiolite high-efficiency dephosphorization adsorbing material with the functional component of amorphous cerium-iron nano particles.
Example 3:
2 g of sepiolite, 1.31 g of cerous nitrate hexahydrate, 0.82 g of ferric chloride hexahydrate and 9 g of urea are dissolved in 100 mL of water and placed on a magnetic stirrer to be stirred for 1 hour; after the solution is uniformly mixed, 1 g of ascorbic acid is added into the solution, and the solution is continuously stirred for 0.4 h; then heating and stirring at 85 ℃ for reaction for 4 hours, and controlling the rotating speed at 500 r/min. After the reaction is finished, the product is subjected to solid-liquid separation and cleaning for a plurality of times, and is dried for 12 hours at 50 ℃ to obtain the modified sepiolite high-efficiency dephosphorization adsorbing material with the functional component of amorphous cerium-iron nano particles.
Example 4:
dissolving 2 g halloysite, 1.74 g cerous nitrate hexahydrate, 0.56 g ferric chloride hexahydrate and 7.2 g urea in 100 mL water, and mechanically stirring for 2 h; after the solution is uniformly mixed, 0.65 g of ascorbic acid is added into the solution, and the solution is continuously stirred for 0.5 h; then heating and stirring the mixture at 85 ℃ for reaction for 6 hours, and controlling the rotating speed to be 600 r/min. And after the reaction is finished, performing solid-liquid separation on the product, washing the product for a plurality of times by using water, and drying the product for 12 hours at 50 ℃ to obtain the modified halloysite high-efficiency dephosphorization adsorbing material with the functional component of amorphous cerium-iron nano particles.
Example 5:
2 g of bentonite, 0.87 g of cerous nitrate hexahydrate, 1.08 g of ferric chloride hexahydrate and 9 g of urea are dissolved in 100 mL of water and mechanically stirred for 2 hours; after the solution is uniformly mixed, adding 1.25 g of ascorbic acid into the solution, and continuously stirring the solution for 1 hour; then heating and stirring the mixture at 85 ℃ for reaction for 6 hours, and controlling the rotating speed to be 600 r/min. And after the reaction is finished, performing solid-liquid separation on the product, washing the product for a plurality of times by using water, and drying the product for 12 hours at 50 ℃ to obtain the modified bentonite high-efficiency phosphorus removal adsorbing material with the functional components of amorphous cerium-iron nano particles.
Example 6:
2 g of bentonite, 1.74 g of cerous nitrate hexahydrate, 1.08 g of ferric chloride hexahydrate and 12 g of urea are dissolved in 100 mL of pure water and placed on a magnetic stirrer to be stirred for 2 hours; after the solution is uniformly mixed, adding 1.25 g of ascorbic acid into the solution, and continuously stirring the solution for 1 hour; then heating and stirring the mixture at 85 ℃ for reaction for 6 hours, and controlling the rotating speed to be 600 r/min. And after the reaction is finished, performing solid-liquid separation on the product, washing the product for a plurality of times by using water, and drying the product for 12 hours at 50 ℃ to obtain the modified bentonite high-efficiency phosphorus removal adsorbing material with the functional components of amorphous cerium-iron nano particles.
The technical solution of the present invention is not limited thereto, and other embodiments are not listed herein.
Fig. 1 is an XRD chart of the efficient phosphorus removal and adsorption material of amorphous cerium-iron co-modified sepiolite and natural clay mineral prepared in examples 2 and 3, and it can be seen from the XRD chart that the crystal structure of the efficient phosphorus removal and adsorption material of cerium-iron nano particle co-modified sepiolite and natural clay mineral prepared in examples 2 and 3 is the same as that of the sepiolite. This shows that the loaded cerium carbonate and ferrous carbonate particles are in an amorphous structure, and the co-loading of the cerium and iron nanoparticles only enables the intensity of each diffraction peak of the sepiolite to show a certain descending trend.
Fig. 2 is an SEM image of the cerium-iron co-modified sepiolite natural clay mineral high-efficiency phosphorus removal adsorbent material obtained in example 3, and it can be seen that the obtained phosphorus removal adsorbent material is composed of nanofiber rods and nanoparticles. The nano fiber rod is sepiolite carrier, the nano particles are amorphous cerium-iron nano particles, and the nano particles are unevenly attached to the surface of the fiber rod-shaped structure.
FIG. 3 is a comparison graph of infrared spectra of raw sepiolite and the cerium-iron co-modified sepiolite natural clay mineral high-efficiency dephosphorization adsorbing material obtained in example 3, and it can be seen that after loading cerium-iron nanoparticles, the concentration of cerium-iron nanoparticles is 1500 cm -1 In the vicinity, triple characteristic absorption peaks of carbonate appear in the obtained phosphorus removal material, which indicates that the loaded cerium and iron nanoparticles are metal carbonate compounds, and the loaded cerium and iron nanoparticles are a mixture of cerium carbonate and ferrous carbonate according to preparation conditions.
The invention aims to investigate the advantages and beneficial achievements of the amorphous cerium-iron co-modified natural clay mineral high-efficiency dephosphorization adsorbing material prepared by the embodiment through the following application examples:
application example 1:
the amorphous cerium-iron co-modified natural clay mineral materials prepared in the above examples 1, 2, 3, 4, 5 and 6 were added to 100 ml of raw sewage which was filtered through a 0.45 μm glass fiber filter membrane in an amount of 0.5 g/L, and the mixture was placed in a constant temperature shaking table and subjected to oscillatory adsorption at 25 ℃ and 200 r/min for 2 hours to measure the concentration of the residual phosphate radical in the solution. The properties of the domestic sewage after membrane passing are shown in table 1, and the phosphorus removal effect of the amorphous cerium-iron co-modified natural clay mineral material is shown in table 2. As shown in the table, although the domestic sewage is complex in composition, more types of coexisting ions and higher in concentration, the prepared amorphous cerium-iron co-modified natural clay mineral material has stronger adsorption capacity on phosphate anions, after two-hour treatment, more than 91% of phosphate can be removed, and for the adsorption material with high cerium content, the removal rate of the phosphate can further reach 99.8%.
TABLE 1 quality characteristic table of primary domestic sewage (0.45 μm glass fiber filter)
Figure DEST_PATH_IMAGE001
TABLE 2 phosphorus removal effect of amorphous Ce-Fe co-modified natural clay mineral high-efficiency phosphorus removal adsorption material
Figure 191418DEST_PATH_IMAGE002
Application example 2:
respectively adding the original sepiolite and the amorphous ferrocenium co-modified sepiolite high-efficiency phosphorus removal adsorbing material prepared in example 3 into two parts of initial phosphorus concentration C 0 KH of 10 mg-P/L 2 PO 4 Adding 0.5 g/L of phosphate into the aqueous solution, placing the aqueous solution in a constant-temperature shaking table, oscillating the aqueous solution at the temperature of 25 ℃ and at the rotating speed of 200 r/min, taking the solution at a certain time interval to measure the residual concentration of phosphate, and drawing a relation graph between the concentration of phosphate in the solution and the adsorption time.
As shown in fig. 4, the concentration of phosphate in the solution added with the amorphous cerium-iron co-modified sepiolite high efficiency phosphorus removal adsorbing material continuously decreases with the passage of time. After the cerium and iron are added to co-modify the high-efficiency phosphorus removal adsorption material for 10 min, the removal rate of phosphorus in the solution can reach 75 percent; after 2h, the removal rate of phosphorus is almost 100%; in contrast, sepiolite has a very limited ability to remove phosphorus, and only 3% of the phosphorus is removed by 2 hours of adsorption.
Application example 3:
respectively adding the original sepiolite and the amorphous cerium-iron co-modified sepiolite high-efficiency phosphorus removal adsorbing material prepared in the example 3 into two parts of initial phosphorus concentration C 0 KH of 5 to 100 mg-P/L 2 PO 4 Adding 0.2 g/L of water solution into the water solution, placing the water solution in a constant temperature shaking table, and oscillating and adsorbing for 24 hours at the temperature of 25 ℃ and the rotating speed of 200 r/min.
As shown in FIG. 5, with the increase of the equilibrium phosphorus concentration, the adsorption capacity of the amorphous cerium-iron co-modified sepiolite high-efficiency phosphorus removal adsorption material firstly increases remarkably and then gradually approaches equilibrium, and the saturated adsorption capacity is 50.23 mg-P/g. The ICP-OES measurement result shows that the cerium content in the dephosphorization adsorbing material is 14.13wt%. Through calculation, the adsorption capacity of the amorphous cerium-iron co-modified sepiolite dephosphorization adsorbing material on phosphorus can reach 355.48 mg-P/g Ce, and cerium sites are fully applied. In comparison, the original sepiolite has obviously insufficient adsorption capacity to phosphorus, and the saturated adsorption capacity is only 5.74 mg-P/g. Therefore, the co-modification of the amorphous cerium-iron metal carbonate greatly improves the adsorption capacity of the original sepiolite.
Application example 4:
the amorphous cerium-iron co-modified sepiolite high-efficiency phosphorus removal adsorbing material prepared in example 3 is respectively added to the initial phosphorus concentration C 0 A majority of KH with the pH value of 20 mg-P/L and the range of 2.43 to 11 2 PO 4 In the water solution, the adding amount of the adsorbing material is 0.2 g/L, the adsorbing material is placed in a constant temperature shaking table and is subjected to oscillation adsorption reaction for 24 hours at the temperature of 25 ℃ and the rotating speed of 200 r/min.
As shown in fig. 6, the change of the solution pH value has a small influence on the phosphorus removal performance of the prepared amorphous cerium-iron co-modified sepiolite high-efficiency phosphorus removal adsorbing material. Within a wider pH value range (3 to 10), the phosphorus removal material has excellent phosphorus removal performance, and the saturated adsorption capacity of the phosphorus removal material is hardly influenced by the pH. The prepared amorphous cerium-iron co-modified sepiolite natural clay mineral high-efficiency phosphorus removal adsorbing material is suitable for various different water bodies, and the removal effect of the water bodies on phosphorus is not influenced by the acidity and alkalinity of the water bodies.
Application example 5:
the amorphous cerium-iron co-modified sepiolite high-efficiency phosphorus removal adsorbing material prepared in example 3 is respectively added to the initial phosphorus concentration C 0 10 mg-P/L, cl - 、NO 3 - 、HCO 3 - 、SO 4 2- And Ca 2+ Multiple KH with ion concentration of 100 mg/L 2 PO 4 In the water solution, the adding amount of the adsorbing material is 0.2 g/L, and the adsorbing material is placed in a constant temperature shaking table and is subjected to oscillation adsorption reaction for 24 hours at the temperature of 25 ℃ and the rotating speed of 200 r/min.
As shown in fig. 7, even if the concentration of the coexisting ions in the solution is 10 times of the concentration of the phosphate anions, the phosphorus removal performance of the prepared amorphous cerium-iron co-modified sepiolite high-efficiency phosphorus removal adsorbing material is hardly affected by the coexisting ions, which indicates that the prepared phosphorus removal adsorbing material has high selectivity and anti-ion interference capability for the phosphate anions, and thus, the application of the phosphorus removal adsorbing material in practical water is facilitated.
Appropriate changes and modifications to the embodiments described above will become apparent to those skilled in the art from the disclosure and guidance of the specification. Therefore, the present invention is not limited to the specific embodiments disclosed and described above, and modifications and variations of the present invention are also intended to fall within the scope of the appended claims.

Claims (8)

1. A preparation method of an amorphous high-efficiency dephosphorization adsorption material is characterized by comprising the following steps: the dephosphorization adsorption material is formed by compounding cerium carbonate and ferrous carbonate nanoparticles with a natural clay mineral material, wherein amorphous cerium carbonate and ferrous carbonate nanoparticles are attached to the structural surface of the natural clay mineral material, the natural clay mineral material is one or more of calcium-rich sepiolite, magnesium-rich sepiolite, halloysite, attapulgite, bentonite, diatomite and kaolin, and the preparation method comprises the following steps: adding untreated natural clay mineral material, cerium salt, ferric salt and urea into water, stirring for 0.5 to 10 hours, and adding a reducing agent; and continuously stirring for 0.3 to 2 hours to uniformly mix, then continuously heating and stirring at 60 to 100 ℃ to react for 2 to 24 hours, after the reaction is finished, carrying out solid-liquid separation on the product, cleaning, and drying at 40 to 80 ℃ to obtain the amorphous efficient phosphorus removal adsorbing material.
2. The preparation method of the amorphous high-efficiency phosphorus removal adsorbing material according to claim 1, characterized by comprising the following steps: the cerium salt is one or more of cerium chloride, cerium nitrate and hydrates thereof; the ferric salt is one or more of ferric chloride, ferric nitrate, ferric sulfate and hydrate thereof.
3. According to claim 1The preparation method of the amorphous high-efficiency dephosphorization adsorption material is characterized by comprising the following steps: the molar ratio of the added cerium salt to the added iron salt is 3:1 to 6; with trivalent cerium ions (Ce) 3+ ) The mass ratio of the cerium salt to the natural clay mineral material is 0.03 to 1:1; the molar ratio of urea to the sum of the total amount of cerium salt and ferric salt is 5-50: 1.
4. the method for preparing the amorphous high-efficiency phosphorus removal adsorbing material according to claim 1, wherein the method comprises the following steps: stirring is needed in the synthesis process, the stirring mode is magnetic stirring or mechanical stirring, and the stirring speed is 400-1000 r/min.
5. The method for preparing the amorphous high-efficiency phosphorus removal adsorbing material according to claim 1, wherein the method comprises the following steps: the reducing agent is one or more of ascorbic acid, hydrazine hydrate and citric acid, and the molar usage ratio of the reducing agent to the ferric salt is 1-5.
6. The method for preparing the amorphous high-efficiency phosphorus removal adsorbing material according to claim 1, wherein the method comprises the following steps: the reaction temperature is 60 to 100 ℃ during synthesis, and the reaction time is 2 to 24 hours.
7. The method for preparing the amorphous high-efficiency phosphorus removal adsorbing material according to claim 1, wherein the method comprises the following steps: the solid-liquid separation is one of centrifugal separation, gravity settling and filtration separation.
8. The application of the adsorbing material obtained by the preparation method of the amorphous high-efficiency phosphorus removal adsorbing material according to any one of claims 1 to 7 in removing phosphorus in various water bodies.
CN202011401625.0A 2020-12-02 2020-12-02 Amorphous high-efficiency phosphorus removal adsorption material, preparation method and water treatment application thereof Active CN112675810B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202011401625.0A CN112675810B (en) 2020-12-02 2020-12-02 Amorphous high-efficiency phosphorus removal adsorption material, preparation method and water treatment application thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202011401625.0A CN112675810B (en) 2020-12-02 2020-12-02 Amorphous high-efficiency phosphorus removal adsorption material, preparation method and water treatment application thereof

Publications (2)

Publication Number Publication Date
CN112675810A CN112675810A (en) 2021-04-20
CN112675810B true CN112675810B (en) 2022-10-11

Family

ID=75447311

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202011401625.0A Active CN112675810B (en) 2020-12-02 2020-12-02 Amorphous high-efficiency phosphorus removal adsorption material, preparation method and water treatment application thereof

Country Status (1)

Country Link
CN (1) CN112675810B (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113996268A (en) * 2021-11-16 2022-02-01 太原理工大学 Supported nano zero-valent iron and cerium adsorbent and synchronous nitrogen and phosphorus removal method thereof

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005144370A (en) * 2003-11-17 2005-06-09 Japan Organo Co Ltd Method for regenerating fluorine or phosphate adsorbent
CN103316624A (en) * 2013-06-08 2013-09-25 华烁科技股份有限公司 Dephosphorization agent and preparation method thereof
CN105749892A (en) * 2016-05-16 2016-07-13 哈尔滨工业大学 Preparation method of sea urchin shaped microspheric lanthanum oxycarbonate adsorbent capable of removing phosphorus from water bodies
KR101694357B1 (en) * 2016-05-09 2017-01-09 주식회사 후소엔지니어링 Method of Manufacturing Coating Carrier for Phosphorus Removal
CN107265548A (en) * 2017-07-05 2017-10-20 盛隆资源再生(无锡)有限公司 A kind of method using the attapulgite depth adsorption and dephosphorization for loading hydrated ferric oxide
CN110694583A (en) * 2019-10-29 2020-01-17 哈尔滨工业大学 Preparation method and application of magnetic recyclable lanthanum oxycarbonate phosphorus removal adsorbent

Family Cites Families (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0810610A (en) * 1994-07-05 1996-01-16 Ishihara Sangyo Kaisha Ltd Phosphorus adsorbent
JP4460370B2 (en) * 2004-06-24 2010-05-12 富田製薬株式会社 Method of recovering phosphorus from phosphorus-containing wastewater using fibers having phosphorus adsorption / desorption ability
JP4247633B2 (en) * 2005-03-29 2009-04-02 戸田工業株式会社 Adsorbent
CN1803274A (en) * 2005-12-06 2006-07-19 昆明理工大学 Preparation method of adsorption agent for sewage denitrification and dephosphorization
CN101249417B (en) * 2008-03-28 2010-12-08 合肥工业大学 Concave-convex bar stone clay-trihydrate alumina/iron nano composite adsorbing agent, preparation and applications
CN104136113A (en) * 2011-10-24 2014-11-05 梅塔材料技术有限责任公司 Porous composite media for removing phosphorus from water
CN103240058A (en) * 2013-05-14 2013-08-14 上海先德净水技术有限公司 Method for preparing lanthanum and iron composite absorbing phosphorous removal agent
CN103877937B (en) * 2014-04-15 2016-03-16 江苏省农业科学院 A kind of improvement charcoal base dephosphorization adsorbent and preparation method
CN104556237B (en) * 2014-12-08 2017-04-19 中国科学院合肥物质科学研究院 Ferrous carbonate hexahedron and preparation method thereof
EP3384941B1 (en) * 2015-11-30 2020-12-23 Toray Industries, Inc. Porous fiber and phosphorus adsorption column
CN108380175B (en) * 2018-02-28 2019-10-22 中国科学院广州地球化学研究所 A kind of carbonic acid gas lanthanum-halloysite composite material and its preparation method and application
CN108314163A (en) * 2018-04-20 2018-07-24 东莞市顶盛环保科技有限公司 A kind of efficient dephosphorization agent
CN109847691A (en) * 2019-03-22 2019-06-07 中国人民大学 A kind of lanthanum iron modified zeolite dephosphorization adsorbent and the preparation method and application thereof
CN110813239A (en) * 2019-12-04 2020-02-21 绍兴文理学院 Preparation method of biochar-loaded lanthanum-doped iron oxide
CN111233253A (en) * 2020-01-16 2020-06-05 深圳市蓝清环境科技工程有限公司 Enhanced phosphorus removal process for phosphorus-containing wastewater

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005144370A (en) * 2003-11-17 2005-06-09 Japan Organo Co Ltd Method for regenerating fluorine or phosphate adsorbent
CN103316624A (en) * 2013-06-08 2013-09-25 华烁科技股份有限公司 Dephosphorization agent and preparation method thereof
KR101694357B1 (en) * 2016-05-09 2017-01-09 주식회사 후소엔지니어링 Method of Manufacturing Coating Carrier for Phosphorus Removal
CN105749892A (en) * 2016-05-16 2016-07-13 哈尔滨工业大学 Preparation method of sea urchin shaped microspheric lanthanum oxycarbonate adsorbent capable of removing phosphorus from water bodies
CN107265548A (en) * 2017-07-05 2017-10-20 盛隆资源再生(无锡)有限公司 A kind of method using the attapulgite depth adsorption and dephosphorization for loading hydrated ferric oxide
CN110694583A (en) * 2019-10-29 2020-01-17 哈尔滨工业大学 Preparation method and application of magnetic recyclable lanthanum oxycarbonate phosphorus removal adsorbent

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
Phosphate Removal by Anion Binding on Functionalized Nanoporous Sorbents;WILAIWAN CHOUYYOK等;《Environ. Sci. Technol.》;20100326;第44卷(第8期);第3073-3078页 *
铈铁吸附剂的制备及其吸附水中磷的性能研究;王莉红;《湿法冶金》;20110930;第30卷(第3期);第258-260页 *

Also Published As

Publication number Publication date
CN112675810A (en) 2021-04-20

Similar Documents

Publication Publication Date Title
Wang et al. Coadsorption of tetracycline and copper (II) onto struvite loaded zeolite–an environmentally friendly product recovered from swine biogas slurry
CN110694583B (en) Preparation method and application of magnetic recyclable lanthanum oxide phosphate removal adsorbent
CN104941574B (en) A kind of inorganic ions modified zeolite composite and its application
CN104888748A (en) Modified meerschaum, preparation method and application thereof
CN101569851A (en) Method for preparing magnetic meerschaum
CN102381691A (en) Preparation method of nano hydroxylapatite adsorbent for absorbing heavy metal ions in waste water
CN103769058A (en) Preparation method of carbonized chitosan adsorbent, adsorbent and application method of absorbent
CN112934164A (en) Magnetic phosphorus removal adsorbent and preparation method and application thereof
CN110560012A (en) Method for removing phosphorus in water by using resin-loaded hydrated iron oxide
CN111804276A (en) Preparation method and application of zirconium hydroxide modified magnetic biochar adsorbing material
CN110394154B (en) Preparation method and application of moso bamboo charcoal/FeMn-LDH composite material
CN112675810B (en) Amorphous high-efficiency phosphorus removal adsorption material, preparation method and water treatment application thereof
US20230125135A1 (en) Lanthanum-iron-loaded carbon nanotube film for environmental restoration, preparation and application thereof
CN101486769A (en) Preparation of amidoxime group bacteria cellulose
CN103769082B (en) The charcoal load activity preparation method of MnOx, product and application
CN113426402B (en) Preparation method and application of lanthanum-aluminum multi-element composite mineral phosphorus removal material
CN104815620A (en) Preparation method of magnetic zeolite
Xiong et al. Low-grade sepiolite with low loading of Na/La salts for simultaneous removal of ammonia and phosphate from wastewater
CN112675804B (en) Hydrated cerium carbonate dephosphorizing adsorbent and preparation method and application thereof
CN102423700B (en) Method for preparing modified kaolin heavy metal ion adsorbent by using magnalium basic salt
CN109529776B (en) Graphene oxide-cerium hydroxide composite material, preparation method and application thereof
CN102886240B (en) Adsorbent for removing toxic element arsenic in water and application thereof
CN113856680B (en) Magnetic carbon-doped spinel copper ferrite catalyst and preparation method and application thereof
CN114426676B (en) Magnetic iron-based MOF microbial carrier material and preparation method thereof
CN113559825B (en) Preparation method, product and application of ZIF-8/sodium bentonite composite material

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