CN116143337A - Method for treating acetone-containing high-fluorine wastewater - Google Patents
Method for treating acetone-containing high-fluorine wastewater Download PDFInfo
- Publication number
- CN116143337A CN116143337A CN202310127798.5A CN202310127798A CN116143337A CN 116143337 A CN116143337 A CN 116143337A CN 202310127798 A CN202310127798 A CN 202310127798A CN 116143337 A CN116143337 A CN 116143337A
- Authority
- CN
- China
- Prior art keywords
- fluorine
- wastewater
- adsorbent
- acetone
- treating
- 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.)
- Withdrawn
Links
- 238000000034 method Methods 0.000 title claims abstract description 64
- 239000011737 fluorine Substances 0.000 title claims abstract description 45
- 229910052731 fluorine Inorganic materials 0.000 title claims abstract description 45
- 239000002351 wastewater Substances 0.000 title claims abstract description 35
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 title claims abstract description 28
- 239000003463 adsorbent Substances 0.000 claims abstract description 24
- 238000001179 sorption measurement Methods 0.000 claims abstract description 20
- 239000012528 membrane Substances 0.000 claims abstract description 15
- 238000001223 reverse osmosis Methods 0.000 claims abstract description 15
- 238000001556 precipitation Methods 0.000 claims abstract description 13
- 238000009388 chemical precipitation Methods 0.000 claims abstract description 11
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 11
- 239000000463 material Substances 0.000 claims abstract description 7
- 238000004062 sedimentation Methods 0.000 claims abstract description 7
- UXVMQQNJUSDDNG-UHFFFAOYSA-L Calcium chloride Chemical compound [Cl-].[Cl-].[Ca+2] UXVMQQNJUSDDNG-UHFFFAOYSA-L 0.000 claims abstract description 4
- 239000001110 calcium chloride Substances 0.000 claims abstract description 4
- 229910001628 calcium chloride Inorganic materials 0.000 claims abstract description 4
- 159000000007 calcium salts Chemical class 0.000 claims abstract description 4
- 238000006115 defluorination reaction Methods 0.000 claims abstract description 4
- 238000000909 electrodialysis Methods 0.000 claims abstract description 4
- 230000001112 coagulating effect Effects 0.000 claims abstract 3
- YCKRFDGAMUMZLT-UHFFFAOYSA-N Fluorine atom Chemical compound [F] YCKRFDGAMUMZLT-UHFFFAOYSA-N 0.000 claims description 32
- 239000000701 coagulant Substances 0.000 claims description 16
- 239000000126 substance Substances 0.000 claims description 11
- AZDRQVAHHNSJOQ-UHFFFAOYSA-N alumane Chemical class [AlH3] AZDRQVAHHNSJOQ-UHFFFAOYSA-N 0.000 claims description 10
- 238000005516 engineering process Methods 0.000 claims description 10
- 239000002904 solvent Substances 0.000 claims description 9
- -1 fluorine ions Chemical class 0.000 claims description 8
- 239000007787 solid Substances 0.000 claims description 6
- KRHYYFGTRYWZRS-UHFFFAOYSA-M Fluoride anion Chemical compound [F-] KRHYYFGTRYWZRS-UHFFFAOYSA-M 0.000 claims description 5
- 230000000694 effects Effects 0.000 claims description 5
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims description 4
- JYIBXUUINYLWLR-UHFFFAOYSA-N aluminum;calcium;potassium;silicon;sodium;trihydrate Chemical compound O.O.O.[Na].[Al].[Si].[K].[Ca] JYIBXUUINYLWLR-UHFFFAOYSA-N 0.000 claims description 4
- 229910001603 clinoptilolite Inorganic materials 0.000 claims description 4
- 239000000084 colloidal system Substances 0.000 claims description 4
- 238000000926 separation method Methods 0.000 claims description 4
- CPLXHLVBOLITMK-UHFFFAOYSA-N Magnesium oxide Chemical class [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 claims description 3
- 239000003513 alkali Substances 0.000 claims description 3
- 229940043430 calcium compound Drugs 0.000 claims description 3
- 150000001674 calcium compounds Chemical class 0.000 claims description 3
- WUKWITHWXAAZEY-UHFFFAOYSA-L calcium difluoride Chemical compound [F-].[F-].[Ca+2] WUKWITHWXAAZEY-UHFFFAOYSA-L 0.000 claims description 3
- 229910001634 calcium fluoride Inorganic materials 0.000 claims description 3
- 239000003651 drinking water Substances 0.000 claims description 3
- 235000020188 drinking water Nutrition 0.000 claims description 3
- 238000005189 flocculation Methods 0.000 claims description 3
- 230000016615 flocculation Effects 0.000 claims description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 claims description 3
- 150000002500 ions Chemical class 0.000 claims description 3
- 239000007788 liquid Substances 0.000 claims description 3
- 150000002681 magnesium compounds Chemical class 0.000 claims description 3
- 229910021645 metal ion Inorganic materials 0.000 claims description 3
- 239000000203 mixture Substances 0.000 claims description 3
- 229920002401 polyacrylamide Polymers 0.000 claims description 3
- 150000003839 salts Chemical class 0.000 claims description 3
- 238000000975 co-precipitation Methods 0.000 claims description 2
- 230000003204 osmotic effect Effects 0.000 claims description 2
- 230000000903 blocking effect Effects 0.000 claims 1
- MYFXBBAEXORJNB-UHFFFAOYSA-N calcium cyanamide Chemical compound [Ca+2].[N-]=C=[N-] MYFXBBAEXORJNB-UHFFFAOYSA-N 0.000 claims 1
- 238000006243 chemical reaction Methods 0.000 claims 1
- 238000011033 desalting Methods 0.000 claims 1
- 238000009792 diffusion process Methods 0.000 claims 1
- 244000144992 flock Species 0.000 claims 1
- 239000012466 permeate Substances 0.000 claims 1
- 239000002244 precipitate Substances 0.000 claims 1
- 238000002360 preparation method Methods 0.000 abstract description 6
- 238000004065 wastewater treatment Methods 0.000 abstract description 5
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 abstract description 4
- 238000010612 desalination reaction Methods 0.000 abstract description 4
- 235000008733 Citrus aurantifolia Nutrition 0.000 abstract description 3
- 235000011941 Tilia x europaea Nutrition 0.000 abstract description 3
- 230000003373 anti-fouling effect Effects 0.000 abstract description 3
- 230000007797 corrosion Effects 0.000 abstract description 3
- 238000005260 corrosion Methods 0.000 abstract description 3
- 230000007547 defect Effects 0.000 abstract description 3
- 239000004571 lime Substances 0.000 abstract description 3
- 229910052761 rare earth metal Inorganic materials 0.000 abstract description 3
- 229910052782 aluminium Inorganic materials 0.000 abstract description 2
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 abstract description 2
- 230000009977 dual effect Effects 0.000 abstract description 2
- 229910052742 iron Inorganic materials 0.000 abstract description 2
- 150000002910 rare earth metals Chemical class 0.000 abstract description 2
- 229910002651 NO3 Inorganic materials 0.000 abstract 1
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 abstract 1
- 238000005345 coagulation Methods 0.000 description 7
- 230000015271 coagulation Effects 0.000 description 7
- 238000001704 evaporation Methods 0.000 description 4
- 230000008020 evaporation Effects 0.000 description 4
- 150000002505 iron Chemical class 0.000 description 4
- DIZPMCHEQGEION-UHFFFAOYSA-H aluminium sulfate (anhydrous) Chemical compound [Al+3].[Al+3].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O DIZPMCHEQGEION-UHFFFAOYSA-H 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 239000003292 glue Substances 0.000 description 2
- 239000010842 industrial wastewater Substances 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 239000011149 active material Substances 0.000 description 1
- KCZFLPPCFOHPNI-UHFFFAOYSA-N alumane;iron Chemical compound [AlH3].[Fe] KCZFLPPCFOHPNI-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000010170 biological method Methods 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000002086 nanomaterial Substances 0.000 description 1
- 230000035515 penetration Effects 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
-
- 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
- C02F1/281—Treatment of water, waste water, or sewage by sorption using inorganic sorbents
-
- 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
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
- C02F1/441—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by reverse osmosis
-
- 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
- C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
- C02F1/469—Treatment of water, waste water, or sewage by electrochemical methods by electrochemical separation, e.g. by electro-osmosis, electrodialysis, electrophoresis
- C02F1/4693—Treatment of water, waste water, or sewage by electrochemical methods by electrochemical separation, e.g. by electro-osmosis, electrodialysis, electrophoresis electrodialysis
-
- 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
- C02F1/48—Treatment of water, waste water, or sewage with magnetic or electric fields
-
- 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
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
- C02F1/5236—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using inorganic agents
-
- 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
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
- C02F1/54—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using organic material
- C02F1/56—Macromolecular compounds
-
- 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
- C02F1/66—Treatment of water, waste water, or sewage by neutralisation; pH adjustment
-
- 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
- C02F2101/12—Halogens or halogen-containing compounds
- C02F2101/14—Fluorine or fluorine-containing compounds
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A20/00—Water conservation; Efficient water supply; Efficient water use
- Y02A20/124—Water desalination
- Y02A20/131—Reverse-osmosis
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
- Water Treatment By Sorption (AREA)
Abstract
Description
技术领域technical field
本发明涉及废水处理技术领域,尤其涉及一种含丙酮高氟废水处理的方法。The invention relates to the technical field of wastewater treatment, in particular to a method for treating wastewater containing acetone and high fluorine.
背景技术Background technique
废水处理就是利用物理、化学和生物的方法对废水进行处理,使废水净化,减少污染,以至达到废水回收、复用,充分利用水资源,氟是地球上分布最广的元素之一,在所有的元素中,氟的丰度列第13位,占地壳构成的0.06-0.09%。氟的化学性质非常活泼几乎能与所有的元素相互作用,因而地壳中的氟大多数以化合物状态存在。Wastewater treatment is to use physical, chemical and biological methods to treat wastewater, purify wastewater, reduce pollution, and achieve wastewater recycling and reuse, making full use of water resources. Fluorine is one of the most widely distributed elements on the earth. Among the elements, the abundance of fluorine ranks 13th, accounting for 0.06-0.09% of the earth's crust. The chemical properties of fluorine are very active and can interact with almost all elements, so most of the fluorine in the earth's crust exists in the form of compounds.
含丙酮高氟废水的处理主要是采用热浓缩工艺,如多效蒸发,该工艺的原理是将含丙酮高氟废水利用热能浓缩后得到浓水和清水,该工艺能耗大,需要占地面积大的大型设备,同时,废水中的氟离子易使设备腐蚀和结垢,降低设备处理效率,增加设备后期维护和保养费用。膜分离技术将膜的有效过滤性能与传统多效蒸发技术有效结合,弥补了传统多效蒸发技术的不足,具有能耗低、质量好、污染少、工艺过程简单、操作简单等特点,已经逐渐替代传统多效蒸发成为业内主流技术,然而现有技术中的膜材料制备工艺复杂,制备成本较高,强度差,耐腐蚀性能差,抗污性能较差,这些缺陷限制了其在高盐废水处理中的应用。The treatment of waste water containing high fluorine in acetone mainly adopts thermal concentration process, such as multi-effect evaporation. The principle of this process is to use heat energy to concentrate waste water containing high fluorine in acetone to obtain concentrated water and clean water. This process consumes a lot of energy and requires an area of Large and large equipment, at the same time, the fluoride ions in the wastewater are easy to corrode and scale the equipment, reduce the treatment efficiency of the equipment, and increase the maintenance and maintenance costs of the equipment. Membrane separation technology effectively combines the effective filtration performance of the membrane with the traditional multi-effect evaporation technology, which makes up for the shortcomings of the traditional multi-effect evaporation technology. It has the characteristics of low energy consumption, good quality, less pollution, simple process, and simple operation. It has gradually Replacing traditional multi-effect evaporation has become the mainstream technology in the industry. However, the preparation process of membrane materials in the prior art is complicated, the preparation cost is high, the strength is poor, the corrosion resistance is poor, and the anti-fouling performance is poor. These defects limit its application in high-salt wastewater. Processing applications.
发明内容Contents of the invention
本发明的目的是提供一种含丙酮高氟废水处理的方法,解决了现有技术中的膜材料制备工艺复杂,制备成本较高,强度差,耐腐蚀性能差,抗污性能较差,这些缺陷限制了其在高盐废水处理中的应用的问题。The purpose of the present invention is to provide a method for the treatment of acetone-containing high-fluorine wastewater, which solves the problems of complex preparation process, high preparation cost, poor strength, poor corrosion resistance and poor anti-fouling performance of membrane materials in the prior art. Defects limit its application in high-salt wastewater treatment.
为了实现上述目的,本发明采用了如下技术方案:In order to achieve the above object, the present invention adopts the following technical solutions:
一种含丙酮高氟废水处理的方法,包括化学沉淀法、反渗透法、混凝沉淀法、吸附法、电渗析法,其中化学沉淀法是采用钙盐沉淀法处理最为普遍,向废水中投加硝石灰、氯化钙,使废水中的F-与Ca2+反响生成CaF2沉淀而除去,在高浓度含氟废水预处理应用中尤为普遍,化学沉淀法方法简单,处理费用低,但存在二次污染问题,且处理效果也不太理想,出水氟化物含量在15~30mg/L围,原理是F-能与Al3+等形成从AlF2+到AlF63-等多种络合物,经沉降而去除F-。A method for treating acetone-containing high-fluorine wastewater, including chemical precipitation, reverse osmosis, coagulation precipitation, adsorption, and electrodialysis. Among them, the chemical precipitation method is the most common calcium salt precipitation method. Add salt lime and calcium chloride to make F- and Ca2+ in the wastewater react to form CaF2 precipitation and remove it, which is especially common in the pretreatment of high-concentration fluorine-containing wastewater. The chemical precipitation method is simple and low in treatment costs, but there are secondary Pollution problem, and the treatment effect is not ideal. The fluoride content in the effluent is around 15-30mg/L. The principle is that F- can form various complexes from AlF2+ to AlF63- with Al3+, and F- can be removed by sedimentation. .
优选的,混凝沉淀法是在含氟废水中参加混凝剂,并用碱调到适当pH,使其形成氢氧化物胶体吸附氟,该法常用的混凝剂可分为两类:一类是无机混凝剂,常采用铝盐、铁盐、钙化合物以及镁化合物,混凝剂投入水中后,其金属离子就会形成细微的胶核或绒絮体,这些絮体吸附氟离子产生共沉淀,从而到达除氟的目的,另一类是有机混凝剂,常用的是聚丙烯酰胺类,该法中铝盐和铁盐混凝法应用最多,适用于工业废水的处理,硫酸铝、聚合铝等铝盐对氟离子都具有较好的混凝去除效果。Preferably, the coagulation-sedimentation method is to add a coagulant in the fluorine-containing wastewater, and adjust it to an appropriate pH with an alkali to form a hydroxide colloid to absorb fluorine. The coagulants commonly used in this method can be divided into two categories: one It is an inorganic coagulant. Aluminum salt, iron salt, calcium compound and magnesium compound are often used. After the coagulant is put into water, its metal ions will form fine glue nuclei or flocs. Precipitation, so as to achieve the purpose of defluoridation, the other is organic coagulant, commonly used is polyacrylamide, in this method, aluminum salt and iron salt coagulation method are most widely used, suitable for the treatment of industrial wastewater, aluminum sulfate, Aluminum salts such as polyaluminum have good coagulation and removal effects on fluoride ions.
优选的,反渗透技术是前些年来迅速开展起来的膜别离技术的一种,反渗透膜选择性的只能透过溶剂而截流离子物质的特性,以膜两侧压力差为推动力,克制溶剂的渗透压,使溶剂通过反渗透而实现对液体混合物进展别离的过程,从本质上来说,该方法没有选择性,只是在除盐过程中将F-也一起去除。Preferably, the reverse osmosis technology is a kind of membrane separation technology that has been developed rapidly in the past few years. The reverse osmosis membrane can only selectively pass through the solvent and intercept ionic substances. The pressure difference on both sides of the membrane is used as the driving force to restrain The osmotic pressure of the solvent is the process of separating the liquid mixture by the solvent through reverse osmosis. In essence, this method has no selectivity, and only removes F- together during the desalination process.
优选的,吸附现象是指在一定条件下,一种物质的分子、原子或离子能自动地附着在固体外表的现象,或者物质在界面层中,浓度自动发生变化的现象,用吸附材料来降氟主要是通过水中F-扩散到固体吸附剂外表,与吸附剂外表键合或只是通过比拟弱的分子间作用力吸附在外表上。Preferably, the adsorption phenomenon refers to the phenomenon that the molecules, atoms or ions of a substance can automatically attach to the surface of the solid under certain conditions, or the phenomenon that the concentration of the substance changes automatically in the interface layer. Fluorine mainly diffuses to the surface of the solid adsorbent through F- in water, bonds with the surface of the adsorbent or is only adsorbed on the surface by relatively weak intermolecular forces.
优选的,吸附铝盐絮凝沉淀除氟过程为静电吸附,且AC或PAC含氟絮体由于吸附了带电荷的氟离子,正电荷被部分中和,相同pH条件下电位要比其本身絮体要低。Preferably, the defluorination process of adsorption of aluminum salt flocculation precipitation is electrostatic adsorption, and because AC or PAC fluorine-containing flocs adsorb charged fluorine ions, the positive charge is partially neutralized, and the potential is higher than that of the flocs themselves under the same pH condition. to be low.
优选的,用于除氟的常用吸附剂主要有活性氧化铝、斜发沸石、活性氧化镁,吸附剂可将氟浓度为10mg/L的废水处理到1mg/L以下,达到饮用水的标准。Preferably, the commonly used adsorbents for fluorine removal mainly include activated alumina, clinoptilolite, and activated magnesia. The adsorbents can treat wastewater with a fluorine concentration of 10 mg/L to below 1 mg/L, reaching the standard for drinking water.
本发明至少具备以下有益效果:The present invention at least has the following beneficial effects:
本发明中的吸附剂的吸附容量偏低,如斜发沸石对氟离子的吸附容量约为,活性氧化铝的吸附容量不超过2mg/g,因此,吸附法中选择适宜的吸附剂非常关键,常用的吸附材料有稀土元素、活性材料、复合材料、纳米材料、铁铝及其化合物等,根据原材料不同,还可将吸附剂分为铁基吸附剂、铝基吸附剂、稀土类吸附剂、生物吸附剂等,反渗透法可以十分有效、可靠地实现高氟苦咸水除氟除盐的双重目的。The adsorption capacity of the adsorbent among the present invention is on the low side, such as the adsorption capacity of clinoptilolite to fluoride ion is about 20 mg/g, and the adsorption capacity of activated alumina is no more than 2mg/g, therefore, it is very critical to select a suitable adsorbent in the adsorption method. Commonly used adsorbent materials include rare earth elements, active materials, composite materials, nanomaterials, iron-aluminum and their compounds, etc. According to different raw materials, adsorbents can also be divided into iron-based adsorbents, aluminum-based adsorbents, rare earth adsorbents, Reverse osmosis can effectively and reliably achieve the dual purpose of defluoridation and desalination of high-fluoride brackish water.
具体实施方式Detailed ways
为了使本发明的目的、技术方案及优点更加清楚明白,以下结合实施例,对本发明进行进一步详细说明。应当理解,此处所描述的具体实施例仅仅用以解释本发明,并不用于限定本发明。In order to make the object, technical solution and advantages of the present invention more clear, the present invention will be further described in detail below in conjunction with the examples. It should be understood that the specific embodiments described here are only used to explain the present invention, not to limit the present invention.
实施例一Embodiment one
包括化学沉淀法、反渗透法、混凝沉淀法、吸附法、电渗析法,其中化学沉淀法是采用钙盐沉淀法处理最为普遍,向废水中投加硝石灰、氯化钙,使废水中的F-与Ca2+反响生成CaF2沉淀而除去,在高浓度含氟废水预处理应用中尤为普遍,化学沉淀法方法简单,处理费用低,但存在二次污染问题,且处理效果也不太理想,出水氟化物含量在15~30mg/L围,原理是F-能与Al3+等形成从AlF2+到AlF63-等多种络合物,经沉降而去除F-。Including chemical precipitation method, reverse osmosis method, coagulation precipitation method, adsorption method, and electrodialysis method, among which the chemical precipitation method is the most common method of calcium salt precipitation, adding salt lime and calcium chloride to the wastewater to make the wastewater The F- and Ca2+ react to form CaF2 precipitation and remove it, which is especially common in the pretreatment application of high-concentration fluorine-containing wastewater. The chemical precipitation method is simple and the treatment cost is low, but there are secondary pollution problems, and the treatment effect is not ideal. The fluoride content in the effluent is around 15-30 mg/L. The principle is that F- can form various complexes from AlF2+ to AlF63- with Al3+, etc., and F- can be removed by sedimentation.
实施例二Embodiment two
混凝沉淀法是在含氟废水中参加混凝剂,并用碱调到适当pH,使其形成氢氧化物胶体吸附氟,该法常用的混凝剂可分为两类:一类是无机混凝剂,常采用铝盐、铁盐、钙化合物以及镁化合物,混凝剂投入水中后,其金属离子就会形成细微的胶核或绒絮体,这些絮体吸附氟离子产生共沉淀,从而到达除氟的目的,另一类是有机混凝剂,常用的是聚丙烯酰胺类,该法中铝盐和铁盐混凝法应用最多,适用于工业废水的处理,硫酸铝、聚合铝等铝盐对氟离子都具有较好的混凝去除效果。The coagulation precipitation method is to add a coagulant to the fluorine-containing wastewater, and adjust it to an appropriate pH with alkali to form a hydroxide colloid to absorb fluorine. The coagulants commonly used in this method can be divided into two categories: one is inorganic mixed Coagulant, aluminum salt, iron salt, calcium compound and magnesium compound are often used. After the coagulant is put into water, its metal ions will form fine glue nuclei or velvet flocs. These flocs absorb fluoride ions and produce coprecipitation, thus To achieve the purpose of defluoridation, the other type is organic coagulant, commonly used is polyacrylamide, in which aluminum salt and iron salt coagulation method are most widely used, suitable for the treatment of industrial wastewater, aluminum sulfate, polyaluminum, etc. Aluminum salts have good coagulation and removal effects on fluoride ions.
实施例三Embodiment Three
反渗透技术是前些年来迅速开展起来的膜别离技术的一种,反渗透膜选择性的只能透过溶剂而截流离子物质的特性,以膜两侧压力差为推动力,克制溶剂的渗透压,使溶剂通过反渗透而实现对液体混合物进展别离的过程,从本质上来说,该方法没有选择性,只是在除盐过程中将F-也一起去除。Reverse osmosis technology is a kind of membrane separation technology that has been developed rapidly in the past few years. The reverse osmosis membrane can only selectively pass through the solvent and intercept ionic substances. The pressure difference on both sides of the membrane is used as the driving force to restrain the penetration of solvents. Pressure, the process of separating the liquid mixture by making the solvent through reverse osmosis, in essence, this method is not selective, but F- is also removed during the desalination process.
实施例四Embodiment Four
吸附现象是指在一定条件下,一种物质的分子、原子或离子能自动地附着在固体外表的现象,或者物质在界面层中,浓度自动发生变化的现象,用吸附材料来降氟主要是通过水中F-扩散到固体吸附剂外表,与吸附剂外表键合或只是通过比拟弱的分子间作用力吸附在外表上。Adsorption phenomenon refers to the phenomenon that molecules, atoms or ions of a substance can automatically attach to the surface of a solid under certain conditions, or the phenomenon that the concentration of a substance changes automatically in the interface layer. The use of adsorption materials to reduce fluorine is mainly F- diffuses to the surface of the solid adsorbent through the water, bonds with the surface of the adsorbent or is only adsorbed on the surface by relatively weak intermolecular forces.
实施例五Embodiment five
吸附铝盐絮凝沉淀除氟过程为静电吸附,且AC或PAC含氟絮体由于吸附了带电荷的氟离子,正电荷被部分中和,相同pH条件下电位要比其本身絮体要低。The defluorination process of adsorption aluminum salt flocculation precipitation is electrostatic adsorption, and AC or PAC fluorine-containing flocs adsorb charged fluorine ions, the positive charge is partially neutralized, and the potential is lower than that of the flocs themselves under the same pH conditions.
用于除氟的常用吸附剂主要有活性氧化铝、斜发沸石、活性氧化镁,吸附剂可将氟浓度为10mg/L的废水处理到1mg/L以下,达到饮用水的标准。Commonly used adsorbents for fluoride removal mainly include activated alumina, clinoptilolite, and activated magnesia. The adsorbents can treat wastewater with a fluorine concentration of 10 mg/L to below 1 mg/L, reaching the standard for drinking water.
以上显示和描述了本发明的基本原理、主要特征和本发明的优点。本行业的技术人员应该了解,本发明不受上述实施例的限制,上述实施例和说明书中描述的只是本发明的原理,在不脱离本发明精神和范围的前提下本发明还会有各种变化和改进,这些变化和改进都落入要求保护的本发明的范围内。本发明要求的保护范围由所附的权利要求书及其等同物界定。The basic principles, main features and advantages of the present invention have been shown and described above. Those skilled in the art should understand that the present invention is not limited by the above-mentioned embodiments. What are described in the above-mentioned embodiments and the description are only the principles of the present invention. Variations and improvements, which fall within the scope of the claimed invention. The scope of protection required by the present invention is defined by the appended claims and their equivalents.
Claims (6)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202310127798.5A CN116143337A (en) | 2023-02-17 | 2023-02-17 | Method for treating acetone-containing high-fluorine wastewater |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202310127798.5A CN116143337A (en) | 2023-02-17 | 2023-02-17 | Method for treating acetone-containing high-fluorine wastewater |
Publications (1)
Publication Number | Publication Date |
---|---|
CN116143337A true CN116143337A (en) | 2023-05-23 |
Family
ID=86361430
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN202310127798.5A Withdrawn CN116143337A (en) | 2023-02-17 | 2023-02-17 | Method for treating acetone-containing high-fluorine wastewater |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN116143337A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN118929816A (en) * | 2024-10-12 | 2024-11-12 | 中安智创环保科技有限公司 | A recyclable defluorination agent and preparation method thereof |
-
2023
- 2023-02-17 CN CN202310127798.5A patent/CN116143337A/en not_active Withdrawn
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN118929816A (en) * | 2024-10-12 | 2024-11-12 | 中安智创环保科技有限公司 | A recyclable defluorination agent and preparation method thereof |
CN118929816B (en) * | 2024-10-12 | 2024-12-24 | 中安智创环保科技有限公司 | Recyclable defluorinating agent and preparation method thereof |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN107459200B (en) | High-salt-content wastewater salinity resource recovery process | |
CN104355473B (en) | A kind of method using electrodialytic technique to carry out power plant desulfurization waste water desalination zero discharge treatment | |
CN104071808B (en) | A kind of Coal Chemical Industry strong brine is separated the method that evaporative crystallization prepares Industrial Salt | |
CN113562924A (en) | Treatment system and method for resource utilization of high-salinity wastewater in ferrous metallurgy | |
US20070039895A1 (en) | Process for treating concentrated salt solutions containing doc | |
TWI540103B (en) | Method for removing boron from a boron-containing wastewater | |
CN103663661B (en) | A kind for the treatment of process containing hexavalent chromium trade effluent | |
CN108178408A (en) | A kind of device and method of desulfurization wastewater processing | |
CN108218038A (en) | A method for resin adsorption-desorption-diffusion dialysis treatment of heavy metal-containing wastewater | |
CN104016528A (en) | Method for comprehensively preventing and controlling electrodialytic membrane pollution for desalination of coal chemical brine waste | |
CN106977013B (en) | A kind of purification treatment method of high chlorine-containing thallium waste water and its application | |
EP2792645B1 (en) | Process for removing fluorides from water | |
Zhang et al. | Research on zero discharge treatment technology of mine wastewater | |
CN102351362A (en) | Treatment method for waste water with high chloride ion content in polysilicon production | |
CN116143337A (en) | Method for treating acetone-containing high-fluorine wastewater | |
Chuang et al. | Colloidal silica removal in coagulation processes for wastewater reuse in a high-tech industrial park | |
CN109928475B (en) | Composite water purifying agent and preparation method and application thereof | |
CN108191132A (en) | The recovery method of heavy metal in a kind of high villaumite acid waste water | |
CN113683249B (en) | Method for removing chloride ions in desulfurization wastewater | |
CN107285421B (en) | A method for segmented treatment of acidic fluorine-containing wastewater that is beneficial to sludge recycling | |
Lee et al. | Chloride removal from industrial cooling water using a two-stage ultra-high lime with aluminum process | |
CN114620852A (en) | Treatment method of waste water from CBS process for producing rubber vulcanization accelerator by oxidation method | |
CN205740639U (en) | A kind of strong brine zero discharge treatment device | |
Chuang et al. | Improving the removal of anions by coagulation and dissolved air flotation in wastewater reclamation | |
WO2004046046A1 (en) | Agents for purifying waste water and muddy water |
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 | ||
WW01 | Invention patent application withdrawn after publication | ||
WW01 | Invention patent application withdrawn after publication |
Application publication date: 20230523 |