CN113426402A - Preparation method and application of lanthanum-aluminum multi-element composite mineral phosphorus removal material - Google Patents
Preparation method and application of lanthanum-aluminum multi-element composite mineral phosphorus removal material Download PDFInfo
- Publication number
- CN113426402A CN113426402A CN202110742432.XA CN202110742432A CN113426402A CN 113426402 A CN113426402 A CN 113426402A CN 202110742432 A CN202110742432 A CN 202110742432A CN 113426402 A CN113426402 A CN 113426402A
- Authority
- CN
- China
- Prior art keywords
- lanthanum
- composite mineral
- phosphorus removal
- aluminum
- phosphorus
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- 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
- B01J20/0203—Solid 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
- B01J20/0248—Compounds of B, Al, Ga, In, Tl
-
- 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
- B01J20/12—Naturally occurring clays or bleaching earth
-
- 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
- C02F1/285—Treatment of water, waste water, or sewage by sorption using synthetic organic sorbents
-
- 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
- C02F2101/105—Phosphorus compounds
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Life Sciences & Earth Sciences (AREA)
- Inorganic Chemistry (AREA)
- Analytical Chemistry (AREA)
- Geochemistry & Mineralogy (AREA)
- Dispersion Chemistry (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Water Treatment By Sorption (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
Abstract
The invention belongs to the technical field of environmental material preparation and water quality treatment, and particularly discloses a preparation method and application of a lanthanum-aluminum multi-element composite mineral phosphorus removal material, wherein the preparation method comprises the following steps: 1) uniformly mixing power plant ash and a non-metal mineral material, calcining for 4-5 hours at 600-900 ℃, and cooling to room temperature to obtain a composite mineral material; 2) grinding, sieving and drying the composite mineral material to obtain composite mineral powder; 3) and mixing the composite mineral powder with the lanthanum-aluminum modified alkali liquor to obtain a mixture, and then sequentially carrying out ultrasonic treatment, stirring, filtering and drying on the mixture to obtain the lanthanum-aluminum multi-element composite mineral phosphorus removal material. The lanthanum-aluminum multi-element composite mineral phosphorus removal material is crushed and then packaged and linked in a non-woven fabric filter bag, so that the lanthanum-aluminum multi-element composite mineral phosphorus removal material capable of being recycled can be obtained. The phosphorus removal material is applied to phosphorus-containing sewage and has a good phosphorus removal effect.
Description
Technical Field
The invention relates to the technical field of environmental material preparation and water quality treatment, in particular to a preparation method and application of a lanthanum-aluminum multi-element composite mineral phosphorus removal material.
Background
With the economic development and the increasingly accelerated urbanization process, phosphate pollution in natural water systems and water eutrophication have become major environmental problems threatening various organisms. According to 2016 national environmental condition publication, V-type and poor V-type water bodies account for 5.4% and 8.0% of the monitored 112 national critical control lakes (reservoirs). The main nutrient components causing water eutrophication comprise organic carbon, nitrogen, phosphorus, potassium and the like, the organic carbon in the sewage can be basically removed after general biological treatment, the content of other components except nitrogen and phosphorus is extremely low relative to the demand in the eutrophication occurrence process and cannot become a limiting factor of the eutrophication, therefore, the main factor causing the mass propagation of algae is nitrogen and phosphorus, the phosphorus is an important factor causing the water eutrophication, the water body polluted by the phosphorus and the algae are propagated in large quantities, the decomposition of the dead algae can cause the water body to generate musty taste and odor, many varieties can also generate toxin, and the health of human beings is influenced through a food chain, so the reduction of the phosphorus content in the sewage has important significance.
In recent years, compounds of lanthanum and aluminum have high affinity for phosphorus, and are widely applied to phosphorus removal in water. A lanthanum modified bentonite (Phoslock), as developed by the australian federal scientific and industrial research organization (CSIRO), can reduce phosphate concentrations to trace levels. After many european lakes have been administered aluminum, the phosphorus load within the deposit can be significantly reduced. However, the single lanthanum adsorbent is greatly influenced by organic matters in the water body, the existence of negative charges on the surface is not favorable for attracting phosphate radicals and hydrogen phosphate radicals in the water body, and the price is high. The single aluminum modified adsorbent is easy to acidify the water body, the water body risk is high, the pH value of the used water body is more between 6 and 9, and the water body type is narrow.
In order to further reduce the cost, the development of an environment-friendly, cheap and easily available lanthanum-based and aluminum-based carrier which does not influence the dephosphorization efficiency is a main subject of current research. The power plant ash is used as the discharge of a coal-fired power plant, has large yield, low utilization rate, rich pore structure, certain adsorbability and low price and is easy to obtain. The expanded perlite has good adsorption effect on phosphorus in water due to the unique surface structure and performance, the mineral reserves of attapulgite, montmorillonite and the like are rich, the expanded perlite is widely applied to the field of environmental protection, and the heat-treated calcium-rich attapulgite (TCAP) can adsorb a certain amount of phosphorus. Therefore, the composite mineral phosphorus removal material prepared by using the non-metallic mineral material and the power plant ash through a certain technical means has a certain research value.
Disclosure of Invention
Aiming at the problems and the defects in the prior art, the invention aims to provide a preparation method and application of a lanthanum-aluminum multi-element composite mineral phosphorus removal material.
Based on the purpose, the invention adopts the following technical scheme:
in a first aspect, the invention provides a preparation method of a lanthanum-aluminum multi-element composite mineral phosphorus removal material, which comprises the following steps:
(1) uniformly mixing power plant ash and a non-metal mineral material, calcining for 4-5 hours at 600-900 ℃, and cooling to room temperature to obtain a composite mineral material;
(2) grinding, screening and drying the composite mineral material obtained in the step (1) to obtain composite mineral powder;
(3) and (3) mixing the composite mineral powder obtained in the step (2) with lanthanum-aluminum modified alkali liquor to obtain a mixture, and then sequentially carrying out ultrasonic treatment, stirring, filtering and drying on the mixture to obtain the lanthanum-aluminum multi-element composite mineral phosphorus removal material.
According to the preparation method, the non-metallic mineral material in the step (1) is preferably at least one of attapulgite and expanded perlite.
According to the above production method, preferably, the mass ratio of the power plant ash to the nonmetallic mineral material in step (1) is 1: 5.
According to the preparation method, preferably, the nonmetal mineral material in the step (1) is a mixture of attapulgite and expanded perlite, and the mass ratio of the attapulgite to the expanded perlite in the mixture of the attapulgite and the expanded perlite is 1: 4-4: 1; more preferably, the mass ratio of attapulgite to expanded perlite in the mixture of attapulgite and expanded perlite is 3: 2.
According to the preparation method, preferably, the preparation method of the lanthanum-aluminum modified alkali liquor in the step (3) comprises the following steps: adding LaCl3Solution and AlCl3After the solution is mixed evenly, LaCl is obtained3And AlCl3Mixing the solution, and then adding LaCl3And AlCl3The pH value of the mixed solution is adjusted to 10-12, obtaining lanthanum-aluminum modified alkali liquor; wherein, LaCl3And AlCl3LaCl in mixed solution3With AlCl3The molar ratio of (a) to (b) is 4:1 to 1: 4.
According to the above preparation process, preferably, LaCl3And AlCl3The concentration of the cations in the mixed solution is 0.02-0.2 mol/L. According to the preparation method, preferably, the preparation method of the lanthanum-aluminum modified alkali liquor in the step (3) comprises the following steps: LaCl with cation concentration of 0.02-0.2 mol/L3And AlCl3Adding NaOH or KOH solution with the concentration of 1-2 mol/L into the mixed solution, and adjusting the pH to 10-12; wherein, LaCl3And AlCl3LaCl in mixed solution3With AlCl3In a molar ratio of 4:1, 2:1, 1:2 or 1: 4; more preferably, LaCl3And AlCl3LaCl in mixed solution3With AlCl3Is 1: 1.
According to the above preparation method, the calcination at 850 ℃ for 4 hours is preferably performed in the step (1).
According to the preparation method, the sieving in the step (2) is preferably performed by using a 100-200-mesh sieve; more preferably, a 150 mesh screen is used for the screening.
According to the preparation method, preferably, when the composite mineral powder is mixed with the lanthanum-aluminum modified alkali liquor in the step (3), the dosage of the lanthanum-aluminum modified alkali liquor mixed with the composite mineral powder per gram is 30-60 mL; more preferably, the dosage of the lanthanum-aluminum modified alkali liquor mixed per gram of the composite mineral powder is 50 mL.
According to the preparation method, the ultrasonic time in the step (3) is preferably 2-5 min; stirring for 6-24 h at a stirring speed of 120-150 r/min; the filtration is carried out by using a 0.45 mu m water system filter membrane; the drying temperature is 100-120 ℃; more preferably, the sonication time is 5 min; stirring for 6h at a stirring speed of 150 r/min; the drying temperature was 100 ℃.
In a second aspect, the invention provides a lanthanum-aluminum multi-element composite mineral phosphorus removal material prepared by the preparation method.
In a third aspect, the invention provides an application of the lanthanum-aluminum multi-element composite mineral phosphorus removal material in phosphorus-containing sewage treatment.
According to the application, preferably, the lanthanum-aluminum multi-element composite mineral phosphorus removal material is crushed, packaged and linked in a non-woven fabric filter bag, and then placed in phosphorus-containing sewage for phosphorus adsorption.
Compared with the prior art, the invention has the following positive beneficial effects:
(1) the method comprises the steps of mixing and calcining power plant ash and non-metal mineral materials to obtain a composite mineral material, mixing and stirring the composite mineral material and lanthanum-aluminum modified alkali liquor, and further modifying to obtain the lanthanum-aluminum multi-element composite mineral phosphorus removal material; after the power plant ash and the nonmetal mineral material are mixed and calcined, the surface active components of the power plant ash have interaction, so that the adsorption, chelation and complexation of the lanthanum-aluminum multi-element composite mineral phosphorus removal material on phosphate can be increased, and the lanthanum-aluminum multi-element composite mineral phosphorus removal material has stronger phosphorus adsorption capacity.
(2) The prepared lanthanum-aluminum multi-element composite mineral phosphorus removal material is put into a non-woven fabric filter bag linked by annular fine iron wires and is immersed into a bottom mud solution containing phosphate radicals for phosphorus adsorption, so that on one hand, inorganic phosphorus in a water body is removed in the process of sinking the filter bag; on the other hand, the filter bag covers the surface of the bottom sediment after being sunk into the water body, and continuously reacts with inorganic phosphorus endogenously released by the bottom sediment to form a water-insoluble precipitate, so that the aim of removing phosphorus in water and mud simultaneously can be fulfilled; in addition, phosphate ions penetrate through the filter bag and are combined with the lanthanum-aluminum multi-element composite mineral phosphorus removal material to form surface precipitates, and even in an unfavorable water body environment, the filter bag can still lock phosphorus-containing precipitates in the bag, so that the phosphorus-containing precipitates are prevented from flowing along with waves, and the recessive secondary phosphorus pollution problem is avoided; and the link of the annular iron wire can realize convenient recovery and reutilization of the lanthanum-aluminum multi-element composite mineral phosphorus removal material.
(3) Compared with a commercial phosphorus locking agent, the lanthanum-aluminum multi-element composite mineral phosphorus removal material prepared by the invention has a more effective phosphorus removal effect, and the used raw materials are abundant in reserves, cheap and easily available, environment-friendly, wide in water body adaptation, suitable for large-scale application and wide in research value.
Detailed Description
The present invention is further illustrated by the following specific examples, which do not limit the scope of the invention.
Influence of power plant ash and different non-metallic mineral materials on lanthanum-aluminum multi-element composite mineral phosphorus removal material
In order to discuss the influence of mixing of power plant ash and different non-metallic mineral materials on the phosphorus removal material of the lanthanum-aluminum multi-element composite mineral, experiments of examples 1 to 3 are carried out, and the power plant ash and attapulgite, the power plant ash and expanded perlite, and the power plant ash and attapulgite and expanded perlite are respectively mixed to prepare the phosphorus removal material of the lanthanum-aluminum multi-element composite mineral. Specific contents of examples 1 to 3 are as follows.
Example 1:
a preparation method of a lanthanum-aluminum multi-element composite mineral phosphorus removal material comprises the following steps:
(1) placing 50g of a mixture of power plant ash and attapulgite in a muffle furnace, heating the temperature in the muffle furnace to 850 ℃ at the speed of 10 ℃/min, calcining the mixture at 850 ℃ for 4h, and cooling to room temperature after the calcination is finished to obtain a composite mineral material; wherein the mass ratio of the power plant ash to the attapulgite in the mixture of the power plant ash and the attapulgite is 1: 5;
(2) grinding the composite mineral material obtained in the step (1) in a mortar, sieving with a 150-mesh sieve, and drying in a drying dish to obtain composite mineral powder;
(3) 200mL of 0.1mol/LLaCl3And 0.1mol/LAlCl3Mixing the mixed solution and 1mol/L NaOH solution, pouring the mixed solution into a 1L volumetric flask for constant volume, performing ultrasonic oscillation for 30min to uniformly mix the mixed solution and the NaOH solution, and preparing lanthanum-aluminum modified alkali liquor with the pH value of 10;
(4) mixing the composite mineral powder obtained in the step (2) with the lanthanum-aluminum modified alkali liquor obtained in the step (3) according to the weight ratio of 1 g: and mixing 50mL of the mixture to obtain a mixture, performing ultrasonic treatment on the mixture for 5min, stirring the mixture for 12h at the speed of 150r/min, performing vacuum filtration by using a 0.45-micron water system filter membrane, and drying filter residues in a vacuum drying oven at the temperature of 100 ℃ for 12h to obtain the lanthanum-aluminum multi-element composite mineral phosphorus removal material.
Example 2:
the contents of example 2 are substantially similar to example 1, except that:
and (2) taking 50g of the mixture of the power plant ash and the expanded perlite in the step (1), and placing the mixture in a muffle furnace, wherein the mass ratio of the power plant ash to the expanded perlite in the mixture of the power plant ash and the expanded perlite is 1: 5.
Example 3:
the contents of example 2 are substantially similar to example 1, except that:
taking 50g of the mixture of the power plant ash, the attapulgite and the expanded perlite in the step (1), and placing the mixture in a muffle furnace, wherein the mass ratio of the power plant ash, the attapulgite and the expanded perlite in the mixture of the power plant ash, the attapulgite and the expanded perlite is 1:3: 2.
In order to detect the phosphorus removal efficiency of the lanthanum-aluminum multi-element composite mineral phosphorus removal materials prepared in the embodiments 1 to 3, the phosphorus removal materials prepared in the embodiments 1 to 3 and a commercial phosphorus-locking agent are used for carrying out a phosphorus adsorption experiment, and the adsorption experiment specifically comprises the following steps: 0.1g of phosphorus removal material was added to 100ml of potassium dihydrogen phosphate solution with a concentration of 50mg/L, the mixture was placed on a magnetic stirrer at room temperature in the air for stirring and adsorption, the solution was filtered after 1 hour intervals, and the residual phosphorus concentration was measured in the sampled clear solution, and the results are shown in Table 1.
TABLE 1 adsorption results of La-Al multi-component composite mineral phosphorus removal material prepared from different non-metallic mineral materials and commercial phosphorus-locking agent
As can be seen from table 1, the phosphorus removal effect of the lanthanum-aluminum multi-element composite mineral phosphorus removal material obtained by mixing attapulgite and power plant ash is better than that of the lanthanum-aluminum multi-element composite mineral phosphorus removal material obtained by mixing expanded perlite and power plant ash under the same mixing ratio, but the phosphorus removal effect of the lanthanum-aluminum multi-element composite mineral phosphorus removal material obtained by mixing power plant ash, attapulgite and expanded perlite is slightly better than that of the phosphorus removal material obtained by binary mixing, which may be because the surface active components interact after different non-metallic minerals and power plant ash are mixed and calcined, and the adsorption, chelating and complexing effects of the lanthanum-aluminum multi-element composite mineral phosphorus removal material on phosphate are increased. Meanwhile, as can be seen from table 1, the phosphorus removal effect of the lanthanum-aluminum multi-element composite mineral phosphorus removal material prepared by the invention is better than that of the commercial phosphorus locking agent under the same conditions.
(II) influence of different dosages of power plant ash, attapulgite and expanded perlite on lanthanum-aluminum multi-element composite mineral phosphorus removal material
In order to discuss the influence of the using amounts of the power plant ash, the attapulgite and the expanded perlite on the lanthanum-aluminum multi-element composite mineral phosphorus removal material, experiments of examples 4 to 6 are carried out, and the power plant ash, the attapulgite and the expanded perlite in different proportions are respectively mixed to prepare the lanthanum-aluminum multi-element composite mineral phosphorus removal material. Specific contents of examples 4 to 6 are as follows.
Example 4:
a preparation method of a lanthanum-aluminum multi-element composite mineral phosphorus removal material comprises the following steps:
(1) placing 50g of a mixture of power plant ash, attapulgite and expanded perlite in a muffle furnace, heating the temperature in the muffle furnace to 850 ℃ at a speed of 10 ℃/min, calcining the mixture at 850 ℃ for 4h, and cooling to room temperature after the calcination is finished to obtain a composite mineral material; wherein the mass ratio of the power plant ash, the attapulgite and the expanded perlite in the mixture of the power plant ash, the attapulgite and the expanded perlite is 1:2: 3;
(2) grinding the composite mineral material obtained in the step (1) in a mortar, sieving with a 150-mesh sieve, and drying in a drying dish to obtain composite mineral powder;
(3) 200mL of 0.1mol/LLaCl3And 0.1mol/LAlCl3Mixing the mixed solution and 1mol/L NaOH solution, pouring the mixed solution into a 1L volumetric flask for constant volume, and carrying out ultrasonic oscillation for 30min to uniformly mix the mixed solution and the NaOH solution to obtain lanthanum-aluminum modified alkali liquor with the pH value of 10;
(4) mixing the composite mineral powder obtained in the step (2) with the lanthanum-aluminum modified alkali liquor obtained in the step (3) according to the weight ratio of 1 g: and mixing 50mL of the mixture to obtain a mixture, performing ultrasonic treatment on the mixture for 5min, stirring the mixture for 12h at the speed of 150r/min, performing vacuum filtration by using a 0.45-micron water system filter membrane, and drying filter residues in a vacuum drying oven at the temperature of 100 ℃ for 12h to obtain the lanthanum-aluminum multi-element composite mineral phosphorus removal material.
Example 5:
the contents of example 5 are substantially the same as example 4, except that:
in the step (1), the mass ratio of the power plant ash, the attapulgite and the expanded perlite in the mixture of the power plant ash, the attapulgite and the expanded perlite is 1:1: 4.
Example 6:
the contents of example 6 are substantially the same as those of example 4, except that:
in the step (1), the mass ratio of the power plant ash, the attapulgite and the expanded perlite in the mixture of the power plant ash, the attapulgite and the expanded perlite is 1:4: 1.
In order to detect phosphorus removal efficiency of the lanthanum-aluminum multi-element composite mineral phosphorus removal material prepared from different amounts of power plant ash, attapulgite and expanded perlite, phosphorus adsorption experiments were performed on the lanthanum-aluminum multi-element composite mineral phosphorus removal material prepared in examples 3 and 4 to 6 and a commercial phosphorus locking agent, and the adsorption experiments specifically include the following steps: 0.5g of phosphorus removal material and commercial phosphorus locking agent are respectively added into 100ml of potassium dihydrogen phosphate solution with the concentration of 10mg/L, the solution is placed on a magnetic stirrer at room temperature in the air for stirring and adsorption, the solution is filtered after 1h, and the sampling clear liquid is used for measuring the residual phosphorus concentration, and the results are shown in Table 2.
Table 2 adsorption results of La-Al multi-component composite mineral phosphorus removal material prepared by different mass ratios and commercial phosphorus-locking agent
As can be seen from table 2, in the composite mineral phosphorus removal material, the formula with a large attapulgite content has a relatively better effect of removing phosphorus from a water body, and the formula with a large amount of expanded perlite has a slightly inferior effect of removing phosphorus, and as the proportion of the attapulgite content increases, the phosphorus removal performance of the lanthanum-aluminum multi-element composite mineral phosphorus removal material is improved, and a certain proportion of attapulgite may be added, which is beneficial to optimizing the particle size ratio between the composite mineral phosphorus removal materials.
(III) influence of different stirring time of the composite mineral powder and the lanthanum-aluminum modified alkali liquor on the lanthanum-aluminum multi-element composite mineral phosphorus removal material
In order to discuss the influence of different stirring times of the composite mineral powder and the lanthanum-aluminum modified alkali liquor on the lanthanum-aluminum multi-element composite mineral phosphorus removal material, the experiments of examples 7 to 8 are carried out, and the composite mineral powder and the lanthanum-aluminum modified alkali liquor are respectively mixed and stirred for different times to prepare the lanthanum-aluminum multi-element composite mineral phosphorus removal material. Specific contents of examples 7 to 8 are as follows.
Example 7:
a preparation method of a lanthanum-aluminum multi-element composite mineral phosphorus removal material comprises the following steps:
(1) placing 50g of a mixture of power plant ash, attapulgite and expanded perlite in a muffle furnace, heating the temperature in the muffle furnace to 850 ℃ at a speed of 10 ℃/min, calcining the mixture at 850 ℃ for 4h, and cooling to room temperature after the calcination is finished to obtain a composite mineral material; wherein the mass ratio of the power plant ash, the attapulgite and the expanded perlite in the mixture of the power plant ash, the attapulgite and the expanded perlite is 1:3: 2;
(2) grinding the composite mineral material obtained in the step (1) in a mortar, sieving with a 150-mesh sieve, and drying in a drying dish to obtain composite mineral powder;
(3) 200mL of 0.1mol/LLaCl3And 0.1mol/LAlCl3The mixed solution of (2) and a 1mol/L NaOH solution are mixed and mixed, and the mixed solution is poured into a volume of 1LSetting the volume in a bottle, and ultrasonically oscillating for 30min to uniformly mix the components to obtain lanthanum-aluminum modified alkali liquor with the pH value of 10;
(4) mixing the composite mineral powder obtained in the step (2) with the lanthanum-aluminum modified alkali liquor obtained in the step (3) according to the weight ratio of 1 g: and mixing 50mL of the mixture to obtain a mixture, performing ultrasonic treatment on the mixture for 5min, stirring the mixture for 6h at the speed of 150r/min, performing vacuum filtration by using a 0.45-micron water system filter membrane, and drying filter residues in a vacuum drying oven at the temperature of 100 ℃ for 12h to obtain the lanthanum-aluminum multi-element composite mineral phosphorus removal material.
Example 8:
the contents of example 8 are substantially the same as those of example 7, except that:
in the step (4), after the mixture is subjected to ultrasonic treatment for 5min, stirring for 24h at the speed of 150 r/min.
In order to detect the phosphorus removal efficiency of the lanthanum-aluminum multi-element composite mineral phosphorus removal material prepared by the composite mineral powder and the lanthanum-aluminum modified alkali liquor in different stirring times, phosphorus adsorption experiments are carried out by using the lanthanum-aluminum multi-element composite mineral phosphorus removal material prepared in the embodiments 3, 7 and 8 and a commercial phosphorus locking agent, and the adsorption experiments specifically comprise the following steps: 0.5g of phosphorus removal material and commercial phosphorus locking agent are respectively added into 100ml of potassium dihydrogen phosphate solution with the concentration of 10mg/L, the solution is placed on a magnetic stirrer at room temperature in the air for stirring and adsorption, the solution is filtered after 1h, and the residual phosphorus concentration of sampled clear liquid is measured, and the results are shown in Table 3. TABLE 3 adsorption results of La-Al multi-element composite mineral phosphorus removal material prepared from composite mineral powder and La-Al modified alkali solution at different stirring times and commercial phosphorus locking agent
As can be seen from Table 3, the stirring time has little influence on the phosphorus removal material of the lanthanum-aluminum multi-component composite mineral. The impregnation of the composite mineral in the lanthanum-aluminum modified alkali liquor comprises two processes of forming lanthanum hydroxide/aluminum precipitate and depositing the lanthanum hydroxide/aluminum on the surface of the composite mineral. Too short stirring time can cause incomplete cation precipitation or uneven distribution of lanthanum-aluminum multi-element precipitates on the surface of the composite mineral, thereby influencing the adsorption effect of the lanthanum-aluminum multi-element precipitates on phosphate. The phosphorus removal rate reaches 99.7% with stirring time of 6h, which indicates that lanthanum-aluminum multi-element precipitates are basically formed and uniformly distributed on the surface of the composite mineral, and the stirring time is continuously increased, so that the phosphorus removal rate is over 99%, the phosphorus removal rate is better than that of a commercial phosphorus-locking agent, and the stirring time is not more than 6h in consideration of system errors and time cost.
Influence of dosage ratio of lanthanum-aluminum modified alkali liquor and composite mineral powder on phosphorus removal effect of lanthanum-aluminum multi-element composite mineral phosphorus removal material
In order to study the influence of the dosage ratio of the lanthanum-aluminum modified alkali liquor and the composite mineral powder on the phosphorus removal effect of the lanthanum-aluminum multi-component composite mineral phosphorus removal material, experiments of examples 9 to 11 are carried out, and the composite mineral powder and the lanthanum-aluminum modified alkali liquor are respectively mixed according to different dosage ratios to prepare the lanthanum-aluminum multi-component composite mineral phosphorus removal material. Specific contents of examples 9 to 11 are as follows.
Example 9:
the contents of example 9 are substantially the same as those of example 7, except that:
in the step (4), mixing the composite mineral powder obtained in the step (2) and the lanthanum-aluminum modified alkali liquor obtained in the step (3) according to the weight ratio of 1 g: 30mL of the mixture was mixed to obtain a mixture.
Example 10:
the contents of example 10 are substantially the same as those of example 7, except that:
in the step (4), mixing the composite mineral powder obtained in the step (2) and the lanthanum-aluminum modified alkali liquor obtained in the step (3) according to the weight ratio of 1 g: 40mL of the mixture was mixed to obtain a mixture.
Example 11:
the contents of example 11 are substantially the same as those of example 7, except that:
in the step (4), mixing the composite mineral powder obtained in the step (2) and the lanthanum-aluminum modified alkali liquor obtained in the step (3) according to the weight ratio of 1 g: 60mL of the mixture was mixed to obtain a mixture.
In order to study the influence of the dosage of the lanthanum-aluminum modified alkali liquor and the composite mineral powder on the phosphorus removal effect of the lanthanum-aluminum multi-component composite mineral phosphorus removal material, phosphorus adsorption experiments are performed on the lanthanum-aluminum multi-component composite mineral phosphorus removal material prepared in example 7 and examples 9 to 11, and the specific experimental steps of the phosphorus adsorption experiments are as follows: 0.1g of phosphorus removal material was added to 100ml of 10mg/L potassium dihydrogen phosphate solution, the mixture was placed in air at room temperature on a magnetic stirrer for stirring and adsorption, the solution was filtered after 1 hour intervals, and the sample was taken to measure the residual phosphorus concentration, the results of which are shown in Table 4.
TABLE 4 adsorption results of phosphorus removal materials prepared with different dosage ratios of La-Al modified alkali solution to composite mineral powder
As can be seen from Table 4, the phosphorus removal rate of the lanthanum-aluminum multi-element composite mineral phosphorus removal material gradually increases as the dosage of the lanthanum-aluminum modified alkali solution is gradually increased. The dosage ratio of the composite mineral powder to the lanthanum-aluminum modified alkali liquor is 1 g: when the volume of the composite mineral powder is 30ml, the phosphorus removal rate is 85.5 percent, and when the dosage ratio of the composite mineral powder to the lanthanum-aluminum modified alkali liquor is reduced to 1 g: when the phosphorus removal rate is 50ml, the phosphorus removal rate is increased to 99.7%, and then the dosage ratio of the composite mineral powder to the lanthanum-aluminum modified alkali liquor is reduced, so that the phosphorus removal effect is not greatly improved. The dosage ratio of the composite mineral powder to the lanthanum-aluminum modified alkali liquor is an important index influencing the economic cost of modification, and the larger dosage ratio of the composite mineral powder to the lanthanum-aluminum modified alkali liquor can undoubtedly increase the economic cost and influence the practical application of modification. Due to the increase of the dosage of lanthanum and aluminum, active substances loaded on the composite mineral are correspondingly increased, and the active substances have good adsorption effect on phosphate, which is also the reason that the dosage ratio of the composite mineral powder to the lanthanum and aluminum modified alkali liquor is reduced to increase the removal effect of the phosphate.
Influence of pH value of lanthanum-aluminum modified alkali liquor on phosphorus removal effect of phosphorus removal material
In order to study the influence of the pH value of the lanthanum-aluminum modified alkali liquor on the phosphorus removal effect of the lanthanum-aluminum multi-component composite mineral phosphorus removal material, experiments of example 12 and example 13 were performed, and the lanthanum-aluminum multi-component composite mineral phosphorus removal material was prepared by mixing composite mineral powder with lanthanum-aluminum modified alkali liquors with different pH values, respectively. The details of example 12 and example 13 are as follows.
Example 12:
the contents of example 12 are substantially the same as those of example 7, except that:
in the step (3), the amount of the 1mol/L NaOH solution is adjusted to prepare lanthanum-aluminum modified alkali liquor with the pH value of 11.
Example 13:
the contents of example 13 are substantially the same as those of example 7, except that:
in the step (3), the amount of the 1mol/L NaOH solution is adjusted to prepare the lanthanum-aluminum modified alkali solution with the pH value of 12.
In order to study the influence of the pH value of the lanthanum-aluminum modified alkali liquor on the phosphorus removal effect of the lanthanum-aluminum multi-component composite mineral phosphorus removal material, the lanthanum-aluminum multi-component composite mineral phosphorus removal material prepared in the embodiment 7, the embodiment 12 and the embodiment 13 is subjected to an adsorption experiment, and the specific experimental steps of the adsorption experiment are as follows: 0.1g of phosphorus removal material was added to 100ml of 10mg/L potassium dihydrogen phosphate solution, the mixture was placed in air at room temperature on a magnetic stirrer for stirring and adsorption, the solution was filtered after 1 hour intervals, and the sample was taken to measure the residual phosphorus concentration, the results of which are shown in Table 5.
TABLE 5 influence of the pH value of the La-Al modified alkali solution on the phosphorus removal effect of phosphorus removal material
As can be seen from Table 5, the pH value of the lanthanum-aluminum modified alkaline solution is within the range of 10-12, the phosphorus removal rate of the lanthanum-aluminum multi-element composite mineral phosphorus removal material is high, and is more than 99.5%, which means that the surface of the composite mineral is richer in hydroxyl groups under the alkaline condition, and the hydroxyl groups can be combined with positive charges in the modified solution, so that lanthanum-aluminum ions in the modified solution are easily settled down, a precipitate and a coordination complex are generated, and the phosphorus removal effect of the lanthanum-aluminum multi-element composite mineral phosphorus removal material is enhanced.
Influence of lanthanum-aluminum multi-element composite mineral phosphorus removal material on adsorption of different initial phosphorus concentrations
In order to research the adsorption effect of the lanthanum-aluminum multi-element composite mineral phosphorus removal material on different initial phosphorus concentrations, the lanthanum-aluminum multi-element composite mineral phosphorus removal material prepared in example 3 is respectively added into potassium dihydrogen phosphate solutions with the concentrations of 1mg/L, 10mg/L and 50mg/L to carry out an adsorption experiment, and the specific steps are as follows: 0.1g of each of the lanthanum-aluminum multi-element composite mineral phosphorus removal material prepared in example 3 and the commercial phosphorus locking agent was added to 100ml of potassium dihydrogen phosphate solution with the concentration of 1mg/L, 10mg/L and 50mg/L respectively, the solution was placed on a magnetic stirrer at room temperature in the air and stirred for adsorption, the solution was filtered after 1 hour, and the residual phosphorus concentration was measured in the sampled clear solution, and the results are shown in Table 6.
TABLE 6 adsorption results of La-Al multi-element composite mineral phosphorus removal material on different initial phosphorus concentrations
As can be seen from table 6, as the initial phosphorus concentration increases, the phosphorus removal rate of the lanthanum-aluminum multi-element composite mineral phosphorus removal material slightly decreases, but the decrease is small, when the initial phosphorus concentration is increased from 10mg/L to 50mg/L, the phosphorus removal rate of the lanthanum-aluminum multi-element composite mineral phosphorus removal material only decreases from 99.9% to 96.2%, while the commercial phosphorus-locking agent has a good phosphorus removal effect under low-concentration phosphorus, when the phosphorus concentration increases to 50mg/L, the phosphorus removal rate sharply decreases, because when the amount of the phosphorus removal material is unchanged, the unsaturated adsorption sites on the surface of the phosphorus removal material are fixed, the higher the phosphorus concentration is, the fewer the non-adsorbed unsaturated sites are, therefore, when the phosphorus concentration of the commercial phosphorus-locking agent is higher, the non-adsorbed sites on the surface of the commercial phosphorus-locking agent rapidly decrease, and the adsorption sites on the surface of the lanthanum-aluminum multi-element composite phosphorus removal material still have a large amount.
(VII) influence of different lanthanum-aluminum multi-element composite mineral phosphorus removal material adding amounts on phosphorus adsorption
In order to study the phosphorus adsorption effect of different dosage amounts of the lanthanum-aluminum multi-component composite mineral phosphorus removal material, the lanthanum-aluminum multi-component composite mineral phosphorus removal material prepared in example 3 is used for carrying out an adsorption experiment on phosphorus, and the specific experimental steps are as follows: 0.1g, 0.5g and 1g of the phosphorus removal material prepared in example 3 were added to 100ml of a 10mg/L potassium dihydrogen phosphate solution, the solution was stirred and adsorbed at room temperature in air on a magnetic stirrer, the solution was filtered after 1 hour, and the sample was taken to measure the residual phosphorus concentration, and the results are shown in Table 7.
TABLE 7 adsorption results of phosphorus adsorption results of different dosage amounts of La-Al multi-component composite mineral phosphorus removal materials
As can be seen from table 7, when the initial phosphorus concentration is kept unchanged, the dosage of the lanthanum-aluminum multi-element composite mineral phosphorus removal material is increased, the phosphorus removal rate does not change greatly, and is close to 100% of phosphorus removal rate, mainly because when the phosphorus concentration is unchanged, the dosage of the lanthanum-aluminum multi-element composite mineral phosphorus removal material is more, unsaturated adsorption sites on the surface of the lanthanum-aluminum multi-element composite mineral phosphorus removal material are also increased, although the unit adsorption capacity is reduced, the increase of the total adsorption sites can increase the total amount of adsorbed phosphorus, and the dosage of 0.1g can meet the requirement of efficient adsorption of phosphate, so the dosage is increased, and the improvement effect of the phosphorus removal rate is not obvious.
In addition, the lanthanum-aluminum multi-element composite mineral phosphorus removal material prepared by the invention is immersed into the bottom mud solution containing phosphate radicals through the non-woven fabric filter bag connected by the annular fine iron wires, so that on one hand, inorganic phosphorus in a water body is removed in the process of sinking the filter bag; on the other hand, the water body is immersed and then covers the surface of the bottom mud, and the water body continuously reacts with inorganic phosphorus released from the bottom mud endogenously to form water-insoluble precipitate, so that the aim of controlling the cement uniformly is fulfilled; phosphate ions penetrate through the filter bag and are combined with the multielement composite mineral phosphorus removal material to form surface precipitates, and the filter bag can lock the phosphorus-containing precipitates in the bag in an unfavorable water environment, so that the phosphorus-containing precipitates are prevented from flowing along with waves, and the hidden secondary phosphorus pollution problem is avoided; the linkage of the annular iron wire is beneficial to the recovery and the reutilization of the multi-element composite mineral phosphorus removal material.
Claims (10)
1. A preparation method of a lanthanum-aluminum multi-element composite mineral phosphorus removal material is characterized by comprising the following steps:
(1) uniformly mixing power plant ash and a non-metal mineral material, calcining for 4-5 hours at 600-900 ℃, and cooling to room temperature to obtain a composite mineral material;
(2) grinding, screening and drying the composite mineral material obtained in the step (1) to obtain composite mineral powder;
(3) and (3) mixing the composite mineral powder obtained in the step (2) with lanthanum-aluminum modified alkali liquor to obtain a mixture, and then sequentially carrying out ultrasonic treatment, stirring, filtering and drying on the mixture to obtain the lanthanum-aluminum multi-element composite mineral phosphorus removal material.
2. The method according to claim 1, wherein the non-metallic mineral material in step (1) is at least one of attapulgite and expanded perlite.
3. The method according to claim 2, wherein the mass ratio of the power plant ash to the non-metallic mineral material in the step (1) is 1: 5.
4. The preparation method according to claim 3, wherein the non-metallic mineral material in the step (1) is a mixture of attapulgite and expanded perlite, and the mass ratio of the attapulgite to the expanded perlite in the mixture of the attapulgite and the expanded perlite is 1: 4-4: 1.
5. The preparation method of claim 1, wherein the lanthanum-aluminum modified alkali liquor in the step (3) is prepared by the following steps:
adding LaCl3Solution and AlCl3After the solution is mixed evenly, LaCl is obtained3And AlCl3Mixing the solution, and then adding LaCl3And AlCl3Adjusting the pH value of the mixed solution to 10-12 to obtain lanthanum-aluminum modified alkali liquor; wherein, LaCl3And AlCl3LaCl in mixed solution3With AlCl3The molar ratio of (a) to (b) is 4:1 to 1: 4.
6. The method of claim 5, wherein the LaCl is3And AlCl3The concentration of the cations in the mixed solution is 0.02-0.2 mol/L.
7. The preparation method of claim 1, wherein when the composite mineral powder is mixed with the lanthanum-aluminum modified alkali liquor in the step (3), the dosage of the lanthanum-aluminum modified alkali liquor mixed per gram of the composite mineral powder is 30-60 mL.
8. The preparation method according to claim 1, wherein the ultrasonic time in the step (3) is 2-5 min; stirring for 6-24 h at a stirring speed of 120-150 r/min; the filtration is carried out by using a 0.45 mu m water system filter membrane; the drying temperature is 100-120 ℃.
9. A lanthanum-aluminum multi-element composite mineral phosphorus removal material prepared by the preparation method of any one of claims 1 to 8.
10. The use of the lanthanum-aluminum multi-element composite mineral phosphorus removal material of claim 9 in the treatment of phosphorus-containing wastewater.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202110742432.XA CN113426402B (en) | 2021-07-01 | 2021-07-01 | Preparation method and application of lanthanum-aluminum multi-element composite mineral phosphorus removal material |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202110742432.XA CN113426402B (en) | 2021-07-01 | 2021-07-01 | Preparation method and application of lanthanum-aluminum multi-element composite mineral phosphorus removal material |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN113426402A true CN113426402A (en) | 2021-09-24 |
| CN113426402B CN113426402B (en) | 2022-10-25 |
Family
ID=77758414
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202110742432.XA Active CN113426402B (en) | 2021-07-01 | 2021-07-01 | Preparation method and application of lanthanum-aluminum multi-element composite mineral phosphorus removal material |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN113426402B (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113860907A (en) * | 2021-11-23 | 2021-12-31 | 华北电力大学 | Preparation method of lanthanum-aluminum bimetal modified bentonite ceramsite for water dephosphorization |
| CN114177881A (en) * | 2021-12-06 | 2022-03-15 | 中科智清生态技术(苏州)有限公司 | Lanthanum-alumina material for removing total phosphorus in river and preparation method thereof |
| CN115739017A (en) * | 2022-11-01 | 2023-03-07 | 武汉工程大学 | Preparation method and application of mesoporous lanthanum modified mineral-based efficient phosphorus removal ceramsite |
Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101898058A (en) * | 2010-07-22 | 2010-12-01 | 淮阴工学院 | Preparation method of low-temperature sintered attapulgite-based direct drinking water filter material |
| CN102008936A (en) * | 2010-12-25 | 2011-04-13 | 河南科技大学 | Method for preparing phosphorus adsorbing material from fly ash |
| 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 |
| CN109574104A (en) * | 2018-12-07 | 2019-04-05 | 中国科学院南京地理与湖泊研究所 | A kind of bimetallic wind resistance wave type lock phosphate material and its preparation method and application |
| CN110683596A (en) * | 2019-10-09 | 2020-01-14 | 中国科学院南京地理与湖泊研究所 | Production method for realizing phosphorus fixation capacity amplification of clay mineral |
| CN111097373A (en) * | 2018-10-25 | 2020-05-05 | 中国科学院生态环境研究中心 | Porous adsorption material, oxygen-carrying and adsorption composite functional material and application thereof |
| CN111701578A (en) * | 2020-06-30 | 2020-09-25 | 广西夏阳环保科技有限公司 | Adsorbent for sewage treatment and preparation method thereof |
| CN111905690A (en) * | 2020-08-10 | 2020-11-10 | 重庆大学 | Method for preparing water body nitrogen and phosphorus removal oxygenation composite material by utilizing coal ash |
-
2021
- 2021-07-01 CN CN202110742432.XA patent/CN113426402B/en active Active
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101898058A (en) * | 2010-07-22 | 2010-12-01 | 淮阴工学院 | Preparation method of low-temperature sintered attapulgite-based direct drinking water filter material |
| CN102008936A (en) * | 2010-12-25 | 2011-04-13 | 河南科技大学 | Method for preparing phosphorus adsorbing material from fly ash |
| 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 |
| CN111097373A (en) * | 2018-10-25 | 2020-05-05 | 中国科学院生态环境研究中心 | Porous adsorption material, oxygen-carrying and adsorption composite functional material and application thereof |
| CN109574104A (en) * | 2018-12-07 | 2019-04-05 | 中国科学院南京地理与湖泊研究所 | A kind of bimetallic wind resistance wave type lock phosphate material and its preparation method and application |
| CN110683596A (en) * | 2019-10-09 | 2020-01-14 | 中国科学院南京地理与湖泊研究所 | Production method for realizing phosphorus fixation capacity amplification of clay mineral |
| CN111701578A (en) * | 2020-06-30 | 2020-09-25 | 广西夏阳环保科技有限公司 | Adsorbent for sewage treatment and preparation method thereof |
| CN111905690A (en) * | 2020-08-10 | 2020-11-10 | 重庆大学 | Method for preparing water body nitrogen and phosphorus removal oxygenation composite material by utilizing coal ash |
Non-Patent Citations (1)
| Title |
|---|
| 高耀文: "硅藻土基复合吸附剂的制备及用于富营养化水体除磷的研究", 《中国优秀硕士学位论文全文数据库 工程科技Ⅰ辑》 * |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113860907A (en) * | 2021-11-23 | 2021-12-31 | 华北电力大学 | Preparation method of lanthanum-aluminum bimetal modified bentonite ceramsite for water dephosphorization |
| CN114177881A (en) * | 2021-12-06 | 2022-03-15 | 中科智清生态技术(苏州)有限公司 | Lanthanum-alumina material for removing total phosphorus in river and preparation method thereof |
| CN114177881B (en) * | 2021-12-06 | 2024-05-10 | 中科智清生态技术(苏州)有限公司 | Lanthanum bauxite material for removing total phosphorus in river and preparation method thereof |
| CN115739017A (en) * | 2022-11-01 | 2023-03-07 | 武汉工程大学 | Preparation method and application of mesoporous lanthanum modified mineral-based efficient phosphorus removal ceramsite |
| CN115739017B (en) * | 2022-11-01 | 2024-06-04 | 武汉工程大学 | Preparation method and application of mesoporous lanthanum modified mineral-based efficient dephosphorization ceramsite |
Also Published As
| Publication number | Publication date |
|---|---|
| CN113426402B (en) | 2022-10-25 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN113426402B (en) | Preparation method and application of lanthanum-aluminum multi-element composite mineral phosphorus removal material | |
| CN109317091B (en) | Modified sepiolite heavy metal adsorption material and preparation method thereof | |
| Jing et al. | Behavior of ammonium adsorption by clay mineral halloysite | |
| CN106334518B (en) | A kind of recyclable magnetic phosphorus adsorbent and preparation method thereof | |
| CN105617981A (en) | Sepiolite modification method and application of modified sepiolite to wastewater treatment | |
| CN110560012A (en) | Method for removing phosphorus in water by using resin-loaded hydrated iron oxide | |
| CN112960701A (en) | Schwertmannite for sewage dephosphorization and efficient synthesis method thereof | |
| CN109647351B (en) | Bagasse loaded iron hydroxide adsorbent and preparation method and application thereof | |
| CN112675804B (en) | Hydrated cerium carbonate dephosphorizing adsorbent and preparation method and application thereof | |
| CN113372523B (en) | Transition metal ion modified sulfonic acid covalent organic framework material and preparation and application thereof | |
| CN101691250A (en) | Adsorbing agent for adsorbing phosphate groups and adsorption method | |
| CN113398875A (en) | Preparation method and application of fly ash-based multifunctional adsorbent | |
| CN114797781B (en) | Preparation method of lanthanum-loaded nitrogen-doped porous carbon-phosphorus adsorption material | |
| CN110683596B (en) | Production method for realizing phosphorus fixation capacity amplification of clay mineral | |
| CN110302746B (en) | Composite material for repairing hexavalent chromium polluted water or soil and preparation method thereof | |
| CN1321086C (en) | Modified bentonite chromium remover and its manufacturing method | |
| CN112675810B (en) | Amorphous high-efficiency phosphorus removal adsorption material, preparation method and water treatment application thereof | |
| Wang et al. | Utilizing different types of biomass materials to modify steel slag for the preparation of composite materials used in the adsorption and solidification of Pb in solutions and soil | |
| CN107362776B (en) | Sulfobetaine and inorganic salt composite modified clay, preparation method and application thereof | |
| CN113289572A (en) | Method for preparing heavy metal ion adsorbent by using fly ash aluminum extraction slag | |
| CN113041991A (en) | Preparation method and application of lanthanum-loaded attapulgite phosphorus removal adsorbent | |
| CN106745592B (en) | It is a kind of with heavy metal ion adsorbed and detection function composite flocculation agent and preparation method thereof | |
| CN114196408B (en) | Arsenic-polluted farmland stabilizer, preparation method and application thereof | |
| CN104289175B (en) | A kind of preparation method of polymerizing cationically type thermal activation micropore bimetallic filler | |
| CN107096501B (en) | Iron ion loaded activated carbon for adsorbing xanthate and preparation method and adsorption 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 |