A fluoride removal agent for wastewater and its preparation method
Patent Information
- Authority / Receiving Office
- CN · China
- Patent Type
- Patents(China)
- Current Assignee / Owner
- Filing Date
- 2025-02-12
- Publication Date
- 2026-08-14
AI Technical Summary
[0005]本发明提出一种污水用除氟剂及其制备方法,解决了相关技术中污水用除氟剂除氟率低的问题
本发明中,聚合氯化铝铁作为除氟剂的重要原料,其水解产生的多种高价多核离子能够与氟离子发生络合反应,使氟离子形成沉淀或被吸附在其水解产物的表面,从而有效去除污水中的氟离子。同时,相较于单一的铝盐或铁盐,聚合氯化铝铁在处理复杂水质时具有更广泛的pH适应性和更好的混凝效果,提高除氟率。羧甲基纤维素钠在除氟过程中,能够增加溶液的黏度,使其他除氟成分更好地分散在污水中,保证除氟反应更加均匀、充分地进行。同时,其分子结构中的羧基具有一定的吸附性能,能够与氟离子发生弱相互作用,辅助其他主要除氟成分,增强整体的除氟效果。乙二胺四乙酸铁铵与月桂醇磷酸酯钠协同复配,提高了污水用除氟剂的除氟效果。乙二胺四乙酸具有很强的螯合能力,能够与多种金属离子形成稳定的螯合物,在除氟过程中,它可以与污水中可能存在的干扰金属离子(如钙、镁、铁等)发生螯合反应,防止这些金属离子与氟离子形成难以去除的络合物,从而减少对除氟过程的干扰,使除氟剂能够更有效地作用于氟离子。聚乙二醇具有良好的水溶性和分散性,能够提高除氟剂各成分在污水中的溶解和分散程度,保证各成分与氟离子充分接触,提高反应效率。乙二胺四乙酸与聚乙二醇协同作用,提高了污水用除氟剂的除氟率。
Smart Images

Figure SMS_1
Abstract
Description
Technical Field
[0001] This invention relates to the field of defluoridation technology, specifically to a defluoridation agent for wastewater and its preparation method. Background Technology
[0002] With rapid industrial development, the fluoride content in wastewater discharged from industries such as aluminum electrolysis, steel, phosphate fertilizer, glass, ceramics, and electronics is increasing daily. Simultaneously, in certain geological areas, groundwater may naturally contain high concentrations of fluoride ions. If this fluoride-containing wastewater is discharged directly without effective treatment, it will pose a serious threat to the ecological environment and human health.
[0003] Fluorine is an essential trace element for the human body, but excessive intake can lead to diseases such as dental fluorosis and skeletal fluorosis, affecting the normal development and function of bones and teeth. Environmentally, high concentrations of fluoride ions can negatively impact aquatic ecosystems, interfering with the normal physiological metabolism and reproduction of aquatic organisms and disrupting the ecological balance of water bodies. Traditional fluoride removal methods include precipitation, adsorption, and ion exchange, but these methods often have limitations. Precipitation is not ideal for removing low concentrations of fluoride ions and produces large amounts of sludge; adsorption methods involve difficult and costly adsorbent regeneration; and ion exchange methods have strict requirements for influent water quality and are complex to operate.
[0004] In summary, existing wastewater defluoridation agents have low defluorination rates; therefore, developing highly efficient wastewater defluoridation agents is of significant practical importance. Summary of the Invention
[0005] This invention proposes a defluoridating agent for wastewater and its preparation method, which solves the problem of low defluoridation rate of defluoridating agents for wastewater in related technologies.
[0006] The technical solution of the present invention is as follows: This invention proposes a fluoride removal agent for wastewater, the raw materials of which include the following components by weight: 40-60 parts of polyaluminum ferric chloride, 5-10 parts of sodium carboxymethyl cellulose, 2-20 parts of ferric ammonium ethylenediaminetetraacetate, 5-20 parts of sodium lauryl phosphate, 5-15 parts of ethylenediaminetetraacetic acid, 1-10 parts of polyethylene glycol, and 200-240 parts of water.
[0007] As a further technical solution, the mass ratio of the ferric ammonium ethylenediaminetetraacetate to the sodium lauryl phosphate is 0.5~1.5:1.
[0008] This invention further improves the defluorination rate of wastewater defluorinating agents by adjusting the mass ratio of ferric ammonium ethylenediaminetetraacetate to sodium lauryl phosphate to 0.5~1.5:1.
[0009] As a further technical solution, the mass ratio of ferric ammonium ethylenediaminetetraacetate to sodium lauryl phosphate is 1:1.
[0010] This invention further improves the defluorination rate of wastewater defluorinating agents by adjusting the mass ratio of ferric ammonium ethylenediaminetetraacetate to sodium lauryl phosphate to 1:1.
[0011] As a further technical solution, the mass ratio of ethylenediaminetetraacetic acid to polyethylene glycol is 1~3:1.
[0012] This invention further improves the defluorination rate of wastewater defluorinating agents by adjusting the mass ratio of ethylenediaminetetraacetic acid to polyethylene glycol to 1~3:1.
[0013] As a further technical solution, the mass ratio of ethylenediaminetetraacetic acid to polyethylene glycol is 2:1.
[0014] This invention further improves the defluorination rate of wastewater defluorinating agents by adjusting the mass ratio of ethylenediaminetetraacetic acid to polyethylene glycol to 2:1.
[0015] As a further technical solution, the basicity of the polyaluminum ferric chloride is 60%~90%.
[0016] As a further technical solution, the polyethylene glycol includes one of PEG-800, PEG-1000, and PEG-1500.
[0017] As a further technical solution, the polyethylene glycol is PEG-1000.
[0018] This invention also proposes a method for preparing a defluoridating agent for wastewater, comprising the following steps: S1. Dissolve polyaluminum ferric chloride in water, add sodium carboxymethyl cellulose to obtain the first mixture; S2. After mixing ferric ammonium ethylenediaminetetraacetate and sodium lauryl phosphate, add the first mixture and dissolve to obtain the second mixture; S3. Add ethylenediaminetetraacetic acid and polyethylene glycol to the second mixture, mix well, and obtain a defluorinating agent.
[0019] As a further technical solution, the dissolution temperature in S2 is 35~55℃.
[0020] The working principle and beneficial effects of this invention are as follows: In this invention, polyaluminum ferric chloride (PAFC) serves as a key raw material for defluorination. The various high-valence polynuclear ions generated during its hydrolysis can complex with fluoride ions, causing them to precipitate or be adsorbed onto the surface of its hydrolysis products, thus effectively removing fluoride ions from wastewater. Furthermore, compared to single aluminum or iron salts, PACFC exhibits wider pH adaptability and better coagulation effects when treating complex water qualities, thereby increasing the defluorination rate. Sodium carboxymethyl cellulose (CMC) increases the viscosity of the solution during defluorination, allowing other defluorination components to disperse better in the wastewater, ensuring a more uniform and thorough defluorination reaction. Simultaneously, the carboxyl groups in its molecular structure possess certain adsorption properties, enabling weak interactions with fluoride ions, assisting other key defluorination components and enhancing the overall defluorination effect. The synergistic combination of ferric ammonium ethylenediaminetetraacetate (EDTA) and sodium lauryl phosphate further improves the defluorination effect of wastewater defluorination agents. Ethylenediaminetetraacetic acid (EDTA) possesses strong chelating ability, forming stable chelates with various metal ions. During defluorination, it can chelate with potentially interfering metal ions (such as calcium, magnesium, and iron) in wastewater, preventing these metal ions from forming difficult-to-remove complexes with fluoride ions. This reduces interference with the defluorination process, allowing the defluorinating agent to act more effectively on fluoride ions. Polyethylene glycol (PEG) has good water solubility and dispersibility, improving the solubility and dispersion of each component of the defluorinating agent in wastewater, ensuring sufficient contact between each component and fluoride ions, and increasing reaction efficiency. The synergistic effect of EDTA and PEG enhances the defluorination rate of wastewater defluorinating agents. Detailed Implementation
[0021] The technical solutions of the present invention will be clearly and completely described below with reference to the embodiments of the present invention. Obviously, the described embodiments are only some embodiments of the present invention, and not all embodiments. Based on the embodiments of the present invention, all other embodiments obtained by those of ordinary skill in the art without creative effort are within the scope of protection of the present invention.
[0022] In the following examples and comparative examples, the basicity of polyaluminum ferric chloride is 90%, and the manufacturer is Zhengzhou Chuangshi Water Purification Materials Co., Ltd.; the viscosity of sodium carboxymethyl cellulose is 3100 mPa·s, the degree of substitution is 0.92, and the content is 99.7 wt%; the content of ferric ammonium ethylenediaminetetraacetate is 98 wt%, the content of sodium lauryl phosphate is 98 wt%, the content of ethylenediaminetetraacetic acid is 98 wt%, and the polyethylene glycol is PEG-1000.
[0023] Example 1 A wastewater defluoridating agent comprises the following components by weight: 60 parts polyaluminum ferric chloride, 10 parts sodium carboxymethyl cellulose, 2 parts ferric ammonium ethylenediaminetetraacetate, 20 parts sodium lauryl phosphate, 5 parts ethylenediaminetetraacetic acid, 10 parts polyethylene glycol, and 240 parts water. Its preparation method includes the following steps: S1. Dissolve polyaluminum ferric chloride in water, add sodium carboxymethyl cellulose to obtain the first mixture; S2. After mixing ferric ammonium ethylenediaminetetraacetate and sodium lauryl phosphate, add the first mixture and dissolve at 55°C to obtain the second mixture. S3. Add ethylenediaminetetraacetic acid and polyethylene glycol to the second mixture, mix well, and obtain the defluorinating agent.
[0024] Example 2 A wastewater defluoridating agent comprises the following components by weight: 40 parts polyaluminum ferric chloride, 5 parts sodium carboxymethyl cellulose, 20 parts ferric ammonium ethylenediaminetetraacetic acid, 5 parts sodium lauryl phosphate, 15 parts ethylenediaminetetraacetic acid, 1 part polyethylene glycol, and 200 parts water. Its preparation method includes the following steps: S1. Dissolve polyaluminum ferric chloride in water, add sodium carboxymethyl cellulose to obtain the first mixture; S2. After mixing ferric ammonium ethylenediaminetetraacetate and sodium lauryl phosphate, add the first mixture and dissolve at 35°C to obtain the second mixture. S3. Add ethylenediaminetetraacetic acid and polyethylene glycol to the second mixture, mix well, and obtain the defluorinating agent.
[0025] Example 3 A wastewater defluoridating agent comprises the following components by weight: 50 parts polyaluminum ferric chloride, 8 parts sodium carboxymethyl cellulose, 12 parts ferric ammonium ethylenediaminetetraacetic acid, 6 parts sodium lauryl phosphate, 10 parts ethylenediaminetetraacetic acid, 2 parts polyethylene glycol, and 220 parts water. Its preparation method includes the following steps: S1. Dissolve polyaluminum ferric chloride in water, add sodium carboxymethyl cellulose to obtain the first mixture; S2. After mixing ferric ammonium ethylenediaminetetraacetate and sodium lauryl phosphate, add the first mixture and dissolve at 45°C to obtain the second mixture. S3. Add ethylenediaminetetraacetic acid and polyethylene glycol to the second mixture, mix well, and obtain the defluorinating agent.
[0026] Example 4 The only difference between this embodiment and Embodiment 3 is that the raw materials in this embodiment include the following components by weight: 50 parts of polyaluminum ferric chloride, 8 parts of sodium carboxymethyl cellulose, 4 parts of ferric ammonium ethylenediaminetetraacetate, 14 parts of sodium lauryl phosphate, 10 parts of ethylenediaminetetraacetic acid, 2 parts of polyethylene glycol, and 220 parts of water.
[0027] Example 5 The only difference between this embodiment and embodiment 3 is that the raw materials in this embodiment include the following components by weight: 50 parts of polyaluminum ferric chloride, 8 parts of sodium carboxymethyl cellulose, 6 parts of ferric ammonium ethylenediaminetetraacetate, 12 parts of sodium lauryl phosphate, 10 parts of ethylenediaminetetraacetic acid, 2 parts of polyethylene glycol, and 220 parts of water.
[0028] Example 6 The only difference between this embodiment and Embodiment 3 is that the raw materials in this embodiment include the following components by weight: 50 parts of polyaluminum ferric chloride, 8 parts of sodium carboxymethyl cellulose, 9 parts of ferric ammonium ethylenediaminetetraacetate, 9 parts of sodium lauryl phosphate, 10 parts of ethylenediaminetetraacetic acid, 2 parts of polyethylene glycol, and 220 parts of water.
[0029] Example 7 The difference between this embodiment and Embodiment 3 is that the raw materials in this embodiment include the following components by weight: 50 parts of polyaluminum ferric chloride, 8 parts of sodium carboxymethyl cellulose, 10.8 parts of ferric ammonium ethylenediaminetetraacetate, 7.2 parts of sodium lauryl phosphate, 10 parts of ethylenediaminetetraacetic acid, 2 parts of polyethylene glycol, and 220 parts of water.
[0030] Example 8 The only difference between this embodiment and Example 6 is that the raw materials in this embodiment include the following components by weight: 50 parts of polyaluminum ferric chloride, 8 parts of sodium carboxymethyl cellulose, 9 parts of ferric ammonium ethylenediaminetetraacetate, 9 parts of sodium lauryl phosphate, 4 parts of ethylenediaminetetraacetic acid, 8 parts of polyethylene glycol, and 220 parts of water.
[0031] Example 9 The only difference between this embodiment and Embodiment 6 is that the raw materials in this embodiment include the following components by weight: 50 parts of polyaluminum ferric chloride, 8 parts of sodium carboxymethyl cellulose, 9 parts of ferric ammonium ethylenediaminetetraacetate, 9 parts of sodium lauryl phosphate, 6 parts of ethylenediaminetetraacetic acid, 6 parts of polyethylene glycol, and 220 parts of water.
[0032] Example 10 The only difference between this embodiment and Embodiment 6 is that the raw materials in this embodiment include the following components by weight: 50 parts of polyaluminum ferric chloride, 8 parts of sodium carboxymethyl cellulose, 9 parts of ferric ammonium ethylenediaminetetraacetate, 9 parts of sodium lauryl phosphate, 8 parts of ethylenediaminetetraacetic acid, 4 parts of polyethylene glycol, and 220 parts of water.
[0033] Example 11 The only difference between this embodiment and Embodiment 6 is that the raw materials in this embodiment include the following components by weight: 50 parts of polyaluminum ferric chloride, 8 parts of sodium carboxymethyl cellulose, 9 parts of ferric ammonium ethylenediaminetetraacetate, 9 parts of sodium lauryl phosphate, 9 parts of ethylenediaminetetraacetic acid, 3 parts of polyethylene glycol, and 220 parts of water.
[0034] Comparative Example 1 The only difference between this comparative example and Example 2 is that the raw materials in this comparative example include the following components by weight: 40 parts of polyaluminum ferric chloride, 5 parts of sodium carboxymethyl cellulose, 25 parts of ferric ammonium ethylenediaminetetraacetic acid, 15 parts of ethylenediaminetetraacetic acid, 1 part of polyethylene glycol, and 200 parts of water.
[0035] Comparative Example 2 The only difference between this comparative example and Example 2 is that the raw materials in this comparative example include the following components by weight: 40 parts of polyaluminum ferric chloride, 5 parts of sodium carboxymethyl cellulose, 25 parts of sodium lauryl phosphate, 15 parts of ethylenediaminetetraacetic acid, 1 part of polyethylene glycol, and 200 parts of water.
[0036] Comparative Example 3 The only difference between this comparative example and Example 2 is that the raw materials in this comparative example include the following components by weight: 40 parts of polyaluminum ferric chloride, 5 parts of sodium carboxymethyl cellulose, 15 parts of ethylenediaminetetraacetic acid, 1 part of polyethylene glycol, and 200 parts of water.
[0037] Comparative Example 4 The only difference between this comparative example and Example 2 is that the raw materials in this comparative example include the following components by weight: 40 parts of polyaluminum ferric chloride, 5 parts of sodium carboxymethyl cellulose, 20 parts of ferric ammonium ethylenediaminetetraacetate, 5 parts of sodium lauryl phosphate, 16 parts of ethylenediaminetetraacetic acid, and 200 parts of water.
[0038] Comparative Example 5 The only difference between this comparative example and Example 2 is that the raw materials in this comparative example include the following components by weight: 40 parts of polyaluminum ferric chloride, 5 parts of sodium carboxymethyl cellulose, 20 parts of ferric ammonium ethylenediaminetetraacetate, 5 parts of sodium lauryl phosphate, 16 parts of polyethylene glycol, and 200 parts of water.
[0039] Comparative Example 6 The only difference between this comparative example and Example 2 is that the raw materials in this comparative example include the following components by weight: 40 parts of polyaluminum ferric chloride, 5 parts of sodium carboxymethyl cellulose, 20 parts of ferric ammonium ethylenediaminetetraacetate, 5 parts of sodium lauryl phosphate, and 200 parts of water.
[0040] The wastewater defluoridating agents prepared in Examples 1-11 and Comparative Examples 1-6 were tested according to the following method: Take a batch of wastewater with a fluoride content of 20.0 mg / L, take 10 L of each as a sample, add 15 mL of the defluorinating agent prepared in Examples 1-11 and Comparative Examples 1-6 respectively, stir at 50 rpm for 12 h at room temperature, detect the fluoride content, and calculate the defluorination rate. The specific test data are shown in Table 1.
[0041] The defluorination rate is calculated as follows: A = (20.0 - c1) / c1 × 100%; c1 is the fluorine concentration measured after 12 hours.
[0042]
[0043] Comparing Example 2 with Comparative Examples 1-3, it is shown that the synergistic effect of ferric ammonium ethylenediaminetetraacetate and sodium lauryl phosphate in the present invention improves the defluorination rate of the wastewater defluorinator. Comparing Example 2 with Comparative Examples 4-6, it is shown that the synergistic effect of ethylenediaminetetraacetic acid and polyethylene glycol in the present invention improves the defluorination rate of the wastewater defluorinator.
[0044] Comparing Examples 5-7 with Examples 3-4, it is shown that adjusting the mass ratio of ferric ammonium ethylenediaminetetraacetate (EDTA) to sodium lauryl phosphate to 0.5-1.5:1 further improves the defluorination rate of the wastewater defluorinator. Comparing Example 6 with Examples 5 and 7, it is shown that adjusting the mass ratio of ferric ammonium EDTA to sodium lauryl phosphate to 1:1 in this invention achieves the best defluorination rate improvement for the wastewater defluorinator. Comparing Examples 9-11 with Examples 6 and 8, it is shown that adjusting the mass ratio of EDTA to polyethylene glycol to 1-3:1 in this invention further improves the defluorination rate of the wastewater defluorinator. Comparing Example 10 with Examples 9 and 11, it is shown that adjusting the mass ratio of EDTA to polyethylene glycol to 2:1 in this invention achieves the best defluorination rate improvement for the wastewater defluorinator.
[0045] The above are merely preferred embodiments of the present invention and are not intended to limit the present invention. Any modifications, equivalent substitutions, improvements, etc., made within the spirit and principles of the present invention should be included within the protection scope of the present invention.
Claims
1. A wastewater defluoridating agent, characterized in that, The raw materials include the following components by weight: 40-60 parts of polyaluminum ferric chloride, 5-10 parts of sodium carboxymethyl cellulose, 2-20 parts of ferric ammonium ethylenediaminetetraacetate, 5-20 parts of sodium lauryl phosphate, 5-15 parts of ethylenediaminetetraacetic acid, 1-10 parts of polyethylene glycol, and 200-240 parts of water. The mass ratio of ferric ammonium ethylenediaminetetraacetate to sodium lauryl phosphate is 0.5~1.5:1; The mass ratio of ethylenediaminetetraacetic acid to polyethylene glycol is 1~3:
1.
2. The wastewater defluoridator according to claim 1, characterized in that, The mass ratio of ferric ammonium ethylenediaminetetraacetate to sodium lauryl phosphate is 1:
1.
3. The wastewater defluoridator according to claim 1, characterized in that, The mass ratio of ethylenediaminetetraacetic acid to polyethylene glycol is 2:
1.
4. The wastewater defluoridator according to claim 1, characterized in that, The basicity of the polyaluminum ferric chloride is 60%~90%.
5. The wastewater defluoridator according to claim 1, characterized in that, The polyethylene glycol includes one of PEG-800, PEG-1000, and PEG-1500.
6. The wastewater defluoridator according to claim 5, characterized in that, The polyethylene glycol is PEG-1000.
7. A method for preparing a wastewater defluoridator according to any one of claims 1 to 6, characterized in that, Includes the following steps: S1. Dissolve polyaluminum ferric chloride in water, add sodium carboxymethyl cellulose to obtain the first mixture; S2. After mixing ferric ammonium ethylenediaminetetraacetate and sodium lauryl phosphate, add the first mixture and dissolve to obtain the second mixture; S3. Add ethylenediaminetetraacetic acid and polyethylene glycol to the second mixture, mix well, and obtain a defluorinating agent.
8. The method for preparing a wastewater defluoridating agent according to claim 7, characterized in that, The dissolution temperature described in S2 is 35~55℃.
Citation Information
Patent Citations
Compound medicament for ecological management of rivers and lakes, and preparation method thereof
CN108394942A
Fluorine removal agent, preparation method and fluorine removal method for hydrofluoric acid wastewater
CN114477564A
Coking wastewater fluorine removal agent and application thereof
CN115745113A
Polyaluminum chloride flocculant for softening hard water as well as preparation method and application thereof
CN117800466A
Method for recovering fluorine ions in wastewater
CN118684382A