CN114314798B - Method for removing organic pollutants by activating persulfate through diatomite composite loaded with iron and manganese - Google Patents

Method for removing organic pollutants by activating persulfate through diatomite composite loaded with iron and manganese Download PDF

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CN114314798B
CN114314798B CN202111665617.1A CN202111665617A CN114314798B CN 114314798 B CN114314798 B CN 114314798B CN 202111665617 A CN202111665617 A CN 202111665617A CN 114314798 B CN114314798 B CN 114314798B
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persulfate
manganese
diatomite
iron
composite material
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CN114314798A (en
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张传兵
姜凤成
王明仕
王慧芳
徐亚慧
邱瑶
郭永正
陆兆华
胡进林
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Huaxia Bishui Environmental Protection Technology Co Ltd
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Abstract

The invention relates to a method for removing organic pollutants by activating persulfate through a diatomite composite material loaded with iron and manganese, which comprises the following steps of: (S1) modifying pretreated diatomite by using a mercaptosilane coupling agent, soaking the modified diatomite in a mixed solution of ferrous salt and manganese salt, adding an alkaline solution, stirring to obtain slurry, drying the slurry, washing, drying again, and grinding to obtain an iron and manganese loaded diatomite composite material; and (S2) adding the persulfate aqueous solution and the composite material obtained in the step (S1) into the water body or soil to be repaired, fully mixing, and degrading and removing the organic pollutants in the object to be repaired. The composite material prepared by the invention can effectively activate persulfate and quickly degrade refractory organic matters in a system to be repaired. The method is green, safe, environment-friendly and low in cost, does not need to additionally implement measures such as heating, light irradiation and the like, and saves energy and related equipment.

Description

Method for removing organic pollutants by activating persulfate through diatomite composite loaded with iron and manganese
Technical Field
The invention relates to the field of environmental remediation, in particular to a method for removing organic pollutants by activating persulfate through a diatomite composite loaded with iron and manganese.
Background
In recent years, the problem of water and soil environmental pollution in China is gradually outstanding, and people pay more attention to the pollution. According to the report, shallow groundwater in most cities in China is polluted by organic pollutants in different degrees, about hundreds of thousands of fields exist when industrial plots are shut down and moved, most soil and groundwater have organic pollution, and meanwhile, wastewater discharged by some chemical enterprises contains a certain amount of organic pollutants. The economical and rapid removal of organic contamination from these contaminations is a major and difficult point of remediation.
In recent years, an oxidation technology based on activated persulfate has the advantages of strong oxidation capacity, basically no secondary pollution, easiness in control, low cost and the like, and becomes a hotspot of organic pollution removal research and application, the mechanism of the oxidation technology is that persulfate generates sulfate radicals (formula 1) with strong oxidation property under the activation action of an activator, so that organic pollutants are oxidized and degraded into small molecular substances and finally mineralized into carbon dioxide and water.
S 2 O 8 2- + activator → SO 4 ·- +(SO 4 ·- or SO 4 2- ) (1)
The activators are associated with the cost of the technical application and the presence of secondary pollution to the environment. Therefore, the search for effective activators is an important element for the development of the persulfate advanced oxidation technology. At present, the main activation modes of persulfate mainly comprise thermal activation, light radiation activation, alkali activation and transition metal activation. The thermal activation and the light irradiation activation need extra heating and irradiation equipment, the operation cost is high, the energy consumption is high, the method is only suitable for small-scale soil and water body repair, and the large-area popularization and application cannot be realized at present; the pH needs to be increased to more than 12 for alkali activation, so that the alkali pollution of the soil or water body is repaired; the activation of the transition metal is most commonly performed by ferrous ions, which have high activation efficiency but easily generate a large amount of iron mud, thereby affecting the reutilization of soil or water. And ferrous iron is easily oxidized into ferric iron in the activation process, and then the activity is lost. The biggest defects of the above activation modes are high energy consumption or secondary pollution to the environment caused by the added activating agent. For removing trace organic matters, important is not only that the non-activation effect generates free radicals, but also that the secondary pollution is not generated when removing light-polluted organic matters, and the original state of water or soil is recovered to the greatest extent. Therefore, it is necessary to develop an activating agent for activating persulfate, which has the advantages of low cost, little influence on water or soil environment, easy operation and convenient use, and is used for removing trace organic pollutants.
In the prior art, cysteine and ferrous salt are used together to prolong the activity of the ferric salt.
CN110422922A discloses a method for removing organic pollution by cysteine reinforced iron/persulfate, wherein a mixture of iron ions and cysteine is added into a system to be repaired, and persulfate is oxidized and degraded by the action of the iron ions and the cysteine. However, this method is not economical and requires the consumption of large amounts of cysteine for large scale remediation of water or soil.
CN112023949 discloses a method for degrading printing and dyeing wastewater in monopersulfate, which requires the addition of metal molybdenum salt and metal cobalt salt, even if the lower concentration of cobalt ions is harmful to human bodies and is not easy to discharge in soil, a new pollution source is introduced.
CN112279355A discloses a method for removing antidepressant drugs in water by activating persulfate, which is to add cysteine, ferrous salt and persulfate to oxidize and degrade drug components in water.
The method utilizes the reducibility of cysteine, can improve the utilization rate of ferric salt, and quickly degrades organic substances in a system to be repaired. However, the treatment system has the disadvantages that although the organic pollutant content in the system can be rapidly reduced in a short time, the treatment system has weak effect on the sustained efficacy, often loses activity within a few days, and when new pollution is generated, the treatment system also needs to be added with a medicament again, so that the treatment system is neither economical nor environment-friendly.
In the prior art, carrier-supported iron or an oxide thereof is used as an activating substance, and CN111111741A discloses a porous boron nitride-supported iron nano material, which is prepared by calcining a precursor of cyanuric acid and boric acid at 1400-1600 ℃ in an ammonia atmosphere to obtain porous boron nitride as a carrier, stirring the porous boron nitride with tripotassium iron salt at 80-90 ℃, drying, grinding and calcining at 600-800 ℃. The material has high catalytic activity on persulfate, and the magnetic material can be conveniently separated. On the one hand, the method of the patent needs a plurality of times of calcination, particularly needs calcination at the temperature of more than 1400 ℃, and has serious energy consumption; the material obtained in this patent can be recovered magnetically, but is difficult to recycle and is not economical.
Therefore, the method can not only clear the refractory organic matters of the system to be repaired by using the persulfate-based oxidation technology with high efficiency, but also maintain the efficacy for a long time, and is more convenient for the technical popularization and large-scale application of the persulfate advanced oxidant to practice.
Disclosure of Invention
In view of the above, the implementation of the present invention provides a method for removing organic pollutants in water or soil by using an iron and manganese loaded diatomite composite material to activate persulfate, wherein the method has characteristics of low cost, convenient use and easy operation, and has strong feasibility for repairing organic polluted water or soil. According to the invention, cheap and easily available diatomite is used as a carrier, the modification of the mercaptosilane coupling agent is carried out, the loaded metallic iron is used as an activating substance, the loaded manganese is used as an auxiliary activating substance, and the obtained diatomite loaded with bimetallic iron/manganese is used as a component for activating persulfate, so that persulfate can be efficiently activated, the purpose of long-acting activation is achieved, and the cost is reduced.
The invention provides a method for removing organic pollutants by activating persulfate through a diatomite composite material loaded with iron and manganese, which comprises the following steps of:
(S1) modifying the pretreated diatomite by a mercaptosilane coupling agent, soaking the modified diatomite in a mixed solution of ferrous salt and manganese salt, adding an alkaline solution, stirring to obtain a slurry, drying and washing the slurry, drying again, and grinding to obtain the diatomite composite material loaded with iron and manganese;
and (S2) adding the persulfate aqueous solution and the composite material obtained in the step (S1) into the water body or soil to be repaired, fully mixing, and degrading and removing the organic pollutants in the object to be repaired.
The pretreatment of diatomaceous earth is well known in the art, i.e., diatomaceous earth is soaked in acid, washed with deionized water, and dried, and the acid is not particularly limited, and hydrochloric acid or sulfuric acid is generally used.
Further, the mercaptosilane coupling agent is selected from at least one of KH-580 and KH-590.
Further, the mass ratio of the diatomite to the mercaptosilane coupling agent is 100:4-7. The method for modifying the diatomite by the mercaptosilane coupling agent comprises the following steps: soaking diatomite in an alcoholic solution of a mercaptosilane coupling agent under the reflux condition of 50-60 ℃, taking out, washing with water, and drying to obtain modified diatomite; preferably, the alcoholic solution of mercaptosilane coupling agent has a concentration of 2 to 5% by weight.
The iron and manganese salts are not particularly limited, such as nitrates, halogen salts, and specifically include, but are not limited to, ferrous sulfate, ferrous chloride, ferrous nitrate, manganese chloride. Further, the molar ratio of the ferric salt to the manganese salt is 5-8:1, and the molarity of the ferric salt is 0.2-0.3mol/L.
Preferably, the mass ratio of the modified diatomite to the mixed solution of ferrous salt and manganese salt is 1:3-5.
Further, the alkaline solution is at least one of ammonia water, sodium hydroxide and potassium hydroxide. When the ammonia water is used, the concentration of the ammonia water is 20-30wt%, and when the ammonia water is sodium hydroxide or potassium hydroxide, the mass concentration is 3-5wt%. The addition amount of the alkaline solution is to fully precipitate the ferric salt and the manganese salt.
The washing is with 60-80% ethanol water solution, and the grinding is to 100-200 μm particle size.
Further, the persulfate is selected from the group consisting of sodium peroxodisulfate, potassium peroxodisulfate, and/or ammonium peroxodisulfate, which is selected from the group consisting of sodium peroxodisulfate, potassium peroxodisulfate, and ammonium peroxodisulfate.
The system to be repaired is a body of water or soil, such as groundwater, surface water, wastewater, agricultural soil, industrial contaminated soil, and the like.
Further, in the step (S2), the dosage of the diatomite composite material loaded with iron and manganese is determined according to the system to be repaired and the pollution source therein, and a person skilled in the art can flexibly select the diatomite composite material according to actual needs. For example, for a water body to be treated, 10-30g of diatomite composite material loaded with iron and manganese can be added into each liter of water; the addition amount of the persulfate is 5 to 15 times, preferably 7 to 10 times, the molar amount of the hardly degradable organic pollutant in the object to be treated.
Preferably, a reducing agent can be further added in the step (S2), wherein the reducing agent is at least one of vitamin C, allicin, tea polyphenol, gallic acid, carvacrol, caffeic acid and cysteine, and the adding amount of the reducing agent is 10-20% of the molar amount of the persulfate; the reducing agent is preferably a compound of vitamin C and allicin according to the mass ratio of 1-2:1-2.
The beneficial effects after the implementation of the invention are as follows:
1. compared with the prior art, the invention provides the composite material which utilizes cheap diatomite to load iron and manganese and is used for removing organic matters in water or soil by matching with persulfate. The composite material prepared by the invention can effectively activate persulfate and quickly degrade refractory organic matters in a system to be repaired.
2. According to the invention, the kieselguhr is modified by the mercaptosilane coupling agent, so that the activation capability of the composite material is improved, probably because the loading capability and stability of the kieselguhr to metal are enhanced after the mercaptosilane coupling agent is modified, and also because the mercapto group has certain reducibility, the method is beneficial to the conversion of ferric iron generated in the system back to ferrous iron.
3. The inventor unexpectedly discovers that the addition of a certain amount of manganese and iron can generate a synergistic effect, the durability of the activation performance of the composite material can be obviously improved, and the persulfate is added into the system to be repaired again within a test time of 10 days, so that the composite material still has strong activation performance,
4. the method is green, safe, environment-friendly and low in cost, does not need to additionally implement measures such as heating, light irradiation and the like, saves energy and related equipment, can effectively remove organic pollutants which are difficult to degrade in a system to be repaired, and does not generate secondary pollution to the environment; the application range is wide.
Detailed Description
The present application is further illustrated by the following examples.
Unless otherwise specified, "parts" in the examples of the present invention are parts by mass.
The chlorobenzene concentration in the solution in the embodiment of the invention is obtained by adopting a high performance liquid chromatography test.
Example 1
(S1) soaking 100 parts of diatomite in 10wt% of dilute hydrochloric acid for 1 hour under the stirring condition, centrifuging, drying to finish the pretreatment of the diatomite, soaking the pretreated diatomite in 200 parts of 2wt% KH-580 ethanol solution under the reflux stirring condition at 50 ℃, soaking for 5 hours, taking out, washing with water, and drying to obtain the diatomite modified by the mercaptosilane coupling agent; the modified diatomaceous earth was impregnated with 300 parts of Fe (NO) 3 ) 2 And MnCl 2 In the mixed solution of (1), wherein Fe (NO) 3 ) 2 The molar concentration is 0.2mol/L, mnCl 2 Adding 100 parts of 30wt% ammonia water into the solution with the molar concentration of 0.04mol/L, stirring the solution to form slurry, washing the slurry for 2 times by using deionized water after drying, then washing the slurry for 2 times by using ethanol, drying the slurry, and grinding and sieving the dried slurry to obtain the diatomite composite material loaded with iron and manganese and having the average particle size of about 120 mu m;
(S2) in a 200. Mu.M chlorobenzene brown reagent bottle containing 100mL, 1g of the iron and manganese-loaded diatomite composite obtained in step (S1) and 0.048g of sodium persulfate (molar ratio of sodium persulfate to chlorobenzene is approximately 10: 1) are added to the brown reagent bottle, the bottle is capped and sealed, the reaction bottle is placed on a constant temperature oscillator, and the reaction is started for 1h at 20 ℃ with the chlorobenzene concentration being tested every 15 min.
Example 2
The other conditions and operation were the same as in example 1 except that in step (S1), fe (NO) 3 ) 2 The molar concentration is 0.24mol/L, mnCl 2 The molar concentration is 0.03mol/L.
Example 3
Other conditionsThe same operation as in example 1 was conducted except that in step (S1), fe (NO) 3 ) 2 The molar concentration is 0.24mol/L, mnCl 2 The molar concentration is 0.02mol/L.
Example 4
The other conditions and operation were the same as in example 1 except that in step (S1), fe (NO) 3 ) 2 The molar concentration is 0.16mol/L, mnCl 2 The molar concentration is 0.08mol/L.
Example 5
The other conditions and operation were the same as in example 1 except that in the step (S1), the concentration of the ethanol solution of KH-580 was 3.5wt%.
Example 6
The other conditions and operation were the same as in example 1 except that in the step (S1), the concentration of the ethanol solution of KH-580 was 1.5% by weight.
Example 7
The other conditions and operation were the same as in example 1 except that in the step (S1), the ethanol solution of KH-580 was used in a concentration of 5wt%.
Example 8
The other conditions and operation were the same as in example 1 except that in step (S2), 20. Mu. Mol of vitamin and 20. Mu. Mol of allicin were further added.
Example 9
The other conditions and operations were the same as in example 1 except that in step (S2), 40. Mu. Mol of vitamin was further added.
Example 10
The other conditions and operation were the same as in example 1 except that in step (S2), 40. Mu. Mol of allicin was further added.
Comparative example 1
The other conditions and operation were the same as in example 1 except that in the step (S1), diatomaceous earth was directly impregnated with Fe (NO) without modification with mercaptosilane coupling agent KH-580 3 ) 2 And MnCl 2 In the mixed solution of (1).
Comparative example 2
The other conditions and operation were the same as in example 1 except that in step (S1), mercaptosilane coupling agent KH-580 was replaced with aminosilane coupling agent KH-550 of equal mass.
Comparative example 3
The other conditions and operation were the same as in example 1 except that the modified diatomaceous earth was impregnated with 300 parts of 0.24mol/LFe (NO) 3 ) 2 In solution, i.e. without addition of MnCl 2
Comparative example 4
The other conditions and operation were the same as in example 1 except that the modified diatomaceous earth was impregnated with 300 parts of 0.2mol/L Fe (NO) 3 ) 2 And 0.04mol/L of CuCl 2 In solution.
The concentrations of the chlorobenzene solutions treated with the modified diatomaceous earth and the persulfate in the above examples and comparative examples were measured to calculate the degradation rates. In addition, in order to test the durability of the iron and manganese loaded diatomite composite material of the present invention, the materials were put in batches, specifically, the iron and manganese loaded diatomite composite material was put in the simulated polluted water body first, and was stored away from light, and after 10 days, other reagents, i.e., sodium persulfate, were put in, and in examples 8 to 10, a reducing agent was additionally put in, and the degradation rate after 1 hour of reaction was tested under the same conditions, with the results as shown in table 1 below:
TABLE 1
Figure BDA0003448239210000071
Note: -means that no such test was performed.
As can be seen from the data analysis in Table 1, the diatomite composite material loaded with iron and manganese, which is prepared by the invention, is used as an active substance for activating persulfate, can efficiently activate sodium persulfate so as to degrade organic matters in a water body, purify water quality, and can maintain the effect for a long time, and when the water body needs to be purified again, only persulfate needs to be added again. Or after the purification is finished, the diatomite composite material loaded with iron and manganese and the water system are heterogeneous, so that the diatomite composite material can be taken out for recycling.
According to the invention, the diatomite is modified by the mercaptosilane coupling agent, and then loaded with iron and manganese, so that the synergistic effect can be achieved, the activation capability of the composite material is enhanced together, the stability of the activation capability of the composite material is strong, the composite material is durable, the strong activation capability can be maintained for a long time, and persulfate can be added when the water quality or soil needs to be restored after being polluted again, so that the actual operation is facilitated, and the cost is saved.

Claims (8)

1. A method for removing organic pollutants by activating persulfate through a diatomite composite material loaded with iron and manganese comprises the following steps:
(S1) modifying pretreated diatomite by using a mercaptosilane coupling agent, soaking the modified diatomite in a mixed solution of ferrous salt and manganese salt, adding an alkaline solution, stirring to obtain slurry, drying the slurry, washing, drying again, and grinding to obtain an iron and manganese loaded diatomite composite material; the mass ratio of the diatomite to the mercaptosilane coupling agent is 100:4-7; the molar ratio of the ferrous salt to the manganese salt is 5-8:1, and the molarity of the ferric salt is 0.2-0.3mol/L; the mass ratio of the modified diatomite to the mixed solution of ferrous salt and manganese salt is 1:3-5; the mercaptosilane coupling agent is selected from at least one of KH-580 and KH-590;
(S2) adding the persulfate aqueous solution and the composite material obtained in the step (S1) into the water body or soil to be repaired, fully mixing, and degrading and removing the organic pollutants in the object to be repaired;
and (S2) adding a reducing agent, wherein the reducing agent is a compound of vitamin C and allicin according to a mass ratio of 1-2:1-2, and the adding amount of the reducing agent is 10-20% of the molar amount of persulfate.
2. The method of claim 1, wherein the diatomaceous earth is modified with a mercaptosilane coupling agent by: soaking the diatomite in an alcoholic solution of a mercaptosilane coupling agent under the reflux condition of 50-60 ℃, taking out, washing with water, and drying to obtain modified diatomite; the concentration of the alcoholic solution of the mercaptosilane coupling agent is 2 to 5% by weight.
3. The method according to claim 1, wherein the ferrous and manganese salts are selected from the group consisting of nitrates, halides of the metals.
4. The method according to claim 3, wherein the ferrous salt is selected from the group consisting of ferrous chloride, ferrous nitrate; the manganese salt is selected from manganese nitrate and manganese chloride.
5. The method of claim 1, wherein the alkaline solution is at least one of ammonia, sodium hydroxide, potassium hydroxide; the washing is with 60-80% ethanol water solution, and the grinding is to 100-200 μm particle size.
6. The method according to claim 1, wherein the persulfate is selected from the group consisting of sodium persulfate, potassium persulfate, and ammonium persulfate and/or the persulfate is selected from the group consisting of sodium persulfate, potassium persulfate, and ammonium persulfate and the persulfate is selected from the group consisting of at least one of sodium persulfate, potassium persulfate, and ammonium persulfate.
7. The method according to claim 1, wherein in the step (S2), 1-10g of the diatomite composite loaded with iron and manganese is added per liter of water for the water body to be treated; the addition amount of the persulfate is 10 to 30 times of the molar amount of the organic pollutants difficult to degrade in the object to be treated.
8. The method according to claim 7, wherein in the step (S2), 3-5g of the diatomite composite loaded with iron and manganese is added per liter of water for the water body to be treated; the addition amount of the persulfate is 15 to 20 times of the molar amount of the organic pollutants difficult to degrade in the object to be treated.
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