CN103230705B - Modified ceramic filter material and applications thereof - Google Patents
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Abstract
本发明提供一种改性陶瓷滤料及其应用。该改性陶瓷滤料可由下述方法制备:1)预处理陶瓷滤料;2)配制改性溶液:将环糊精溶解于二甲基甲酰胺溶剂中,得到环糊精溶液;按照环糊精与异氰酸酯的摩尔比为1:7-8将异氰酸酯滴加至反应器中与环糊精溶液混合并搅拌,同时进行紫外光引发;反应结束后对产物进行洗涤、干燥,得到环糊精-异氰酸酯共聚物;按照所述共聚物与水混合,并搅拌得到悬浮物溶液;3)取陶瓷滤料,然后加入步骤2)所得的悬浮物溶液,所述悬浮物溶液的加入量以能封住陶瓷滤料为准,然后搅拌干燥、焙烧,即得到改性陶瓷滤料。此法所得改性陶瓷滤料制备工艺简单,反应迅速,滤料机械强度高,使用寿命长,对氯苯废水处理效果显著,实用性强,前景广泛。The invention provides a modified ceramic filter material and application thereof. The modified ceramic filter material can be prepared by the following methods: 1) pretreatment of the ceramic filter material; 2) preparation of a modified solution: dissolving cyclodextrin in dimethylformamide solvent to obtain a cyclodextrin solution; according to the cyclodextrin The molar ratio of alcohol to isocyanate is 1:7-8. The isocyanate is added dropwise into the reactor, mixed with the cyclodextrin solution and stirred, and at the same time, ultraviolet light is initiated; after the reaction, the product is washed and dried to obtain the cyclodextrin- Isocyanate copolymer; mix the copolymer with water and stir to obtain a suspension solution; 3) Take the ceramic filter material, and then add the suspension solution obtained in step 2), the amount of the suspension solution can be sealed The ceramic filter material shall prevail, then stirred, dried and roasted to obtain the modified ceramic filter material. The modified ceramic filter material obtained by the method has simple preparation process, rapid response, high mechanical strength of the filter material, long service life, remarkable treatment effect of p-chlorobenzene wastewater, strong practicability and broad prospect.
Description
技术领域 technical field
本发明涉及污水处理领域,具体涉及一种改性陶瓷滤料及其应用。 The invention relates to the field of sewage treatment, in particular to a modified ceramic filter material and its application.
背景技术 Background technique
改性滤料即是在载体滤料表面通过物理化学反应涂上一层改性剂,从而改变原滤料表面物理化学性质,从而提高滤料的截污能力,提高滤料对某些特殊物质的吸附能力,改善出水水质。改性陶瓷滤料作为改性滤料在近些年来受到广泛应用。改性剂的研究也有相当大的进展,改性剂的选取应符合易负载、不溶解、无毒无害等条件。目前,改性剂种类繁多,制备方法各异,但仍需进一步探究,找寻制备简单、对有机氯化物利用吸附和过滤方式去除效果显著的改性剂。 The modified filter material is to coat a layer of modifier on the surface of the carrier filter material through physical and chemical reactions, thereby changing the physical and chemical properties of the original filter material surface, thereby improving the ability of the filter material to intercept pollutants, and improving the filter material’s resistance to certain special substances. The adsorption capacity improves the effluent water quality. Modified ceramic filter materials have been widely used as modified filter materials in recent years. The study of modifiers has also made considerable progress. The selection of modifiers should meet the conditions of easy loading, insolubility, non-toxic and harmless. At present, there are many kinds of modifiers and different preparation methods, but further research is still needed to find modifiers that are simple to prepare and have a significant effect on the removal of organic chlorides by adsorption and filtration.
发明内容 Contents of the invention
本发明的目的在于提供一种制备方法简单、对有机氯化物去除效果显著的改性陶瓷滤料及其应用。 The object of the present invention is to provide a modified ceramic filter material with simple preparation method and remarkable effect on removing organic chlorides and its application.
为了实现上述目的,本发明所采用的技术方案是: In order to achieve the above object, the technical solution adopted in the present invention is:
改性陶瓷滤料,其特征在于,它可由下述方法制备: Modified ceramic filter material is characterized in that it can be prepared by the following method:
1)预处理陶瓷滤料:将陶瓷滤料冲洗后HCl溶液浸泡,然后用水冲洗直至冲洗水的pH值接近中性,再将陶瓷滤料干燥; 1) Pretreatment of ceramic filter material: Rinse the ceramic filter material and soak it in HCl solution, then rinse with water until the pH value of the rinse water is close to neutral, and then dry the ceramic filter material;
2)配制改性溶液:将环糊精溶解于二甲基甲酰胺溶剂中,得到环糊精溶液;将所述环糊精溶液加入至反应器内,所述反应器置于30-40℃的水浴中;按照环糊精与异氰酸酯的摩尔比为1:7-8将异氰酸酯滴加至反应器中与环糊精溶液混合并搅拌,同时进行紫外光引发;其中,紫外光的功率为2-6kw,反应8-15分钟;反应结束后对产物进行洗涤、干燥,得到环糊精-异氰酸酯共聚物;按照所述共聚物与水的质量比为0.1-0.15:1将所述共聚物与水混合,并搅拌得到悬浮物溶液,调节所述悬浮物溶液的pH值为6.5-7.5; 2) Prepare modification solution: Dissolve cyclodextrin in dimethylformamide solvent to obtain cyclodextrin solution; add the cyclodextrin solution into the reactor, and place the reactor at 30-40°C in a water bath; according to the molar ratio of cyclodextrin to isocyanate is 1:7-8, isocyanate is added dropwise into the reactor and mixed with the cyclodextrin solution and stirred, and ultraviolet light is initiated at the same time; wherein, the power of ultraviolet light is 2 -6kw, reacted for 8-15 minutes; after the reaction, the product was washed and dried to obtain a cyclodextrin-isocyanate copolymer; according to the mass ratio of the copolymer to water, the copolymer was mixed with mixing with water, and stirring to obtain a suspension solution, adjusting the pH value of the suspension solution to 6.5-7.5;
3)取步骤1)所得的陶瓷滤料,然后加入步骤2)所得的悬浮物溶液,所述悬浮物溶液的加入量以能封住陶瓷滤料为准,然后搅拌、干燥、焙烧,焙烧温度为450-650℃,焙烧时间为2h,即得到改性陶瓷滤料。 3) Take the ceramic filter material obtained in step 1), and then add the suspension solution obtained in step 2). The temperature is 450-650°C, and the firing time is 2 hours, and the modified ceramic filter material can be obtained.
上述方案中,所述步骤1)中的陶瓷滤料的粒径为1.0-1.25mm。 In the above solution, the particle size of the ceramic filter material in step 1) is 1.0-1.25mm.
上述方案中,所述步骤1)中的HCl溶液的浓度为0.1-0.2mol/L,浸泡时间为12-24h。 In the above scheme, the concentration of the HCl solution in step 1) is 0.1-0.2mol/L, and the soaking time is 12-24h.
上述方案中,所述步骤1)中的干燥温度为100-120℃,干燥时间为1-2h。 In the above solution, the drying temperature in step 1) is 100-120° C., and the drying time is 1-2 hours.
上述方案中,所述步骤2)中的异氰酸酯与环糊精溶液混合搅拌的转速为120r/min。 In the above scheme, the rotational speed of mixing and stirring the isocyanate and the cyclodextrin solution in step 2) is 120 r/min.
上述方案中,所述异氰酸酯为六亚甲基二异氰酸酯、二苯基甲烷二异氰酸酯、或甲苯二异氰酸酯。 In the above scheme, the isocyanate is hexamethylene diisocyanate, diphenylmethane diisocyanate, or toluene diisocyanate.
上述改性陶瓷滤料在去除水中氯苯的应用。 Application of the above-mentioned modified ceramic filter material in removing chlorobenzene in water.
上述方案中,所述的改性陶瓷滤料去除水中氯苯的方式为深床过滤。 In the above scheme, the method of removing chlorobenzene in water by the modified ceramic filter material is deep bed filtration.
上述方案中,所述改性陶瓷滤料滤层厚度为150-350mm,滤速为2-8m/h。 In the above scheme, the thickness of the filter layer of the modified ceramic filter material is 150-350mm, and the filtration rate is 2-8m/h.
上述方案中,所述滤层厚度为350mm,滤速为4m/h时。 In the above scheme, the thickness of the filter layer is 350mm, and the filtration rate is 4m/h.
本发明的有益效果在于:紫外光引发合成的异氰酸酯-环糊精共聚物的制备过程中,在高能紫外光的作用下,反应物能迅速被激发出活性基团,加速合成反应的进行,大大缩短常规制备方法所用时间,制备所得共聚物负载于陶瓷滤料表面得到改性陶瓷滤料。此法所得改性陶瓷滤料制备工艺简单,反应速度迅速,滤料机械强度高,使用寿命长,对氯苯废水处理效果显著,实用性强,前景广泛。 The beneficial effect of the present invention is that: in the preparation process of the isocyanate-cyclodextrin copolymer synthesized by ultraviolet light, under the action of high-energy ultraviolet light, the reactants can be rapidly excited out of active groups, which accelerates the progress of the synthesis reaction, greatly The time used in the conventional preparation method is shortened, and the prepared copolymer is loaded on the surface of the ceramic filter material to obtain the modified ceramic filter material. The modified ceramic filter material obtained by the method has the advantages of simple preparation process, rapid reaction speed, high mechanical strength of the filter material, long service life, remarkable treatment effect of p-chlorobenzene wastewater, strong practicability and wide prospect.
具体实施方式 Detailed ways
为了更好地理解本发明,下面结合实施例进一步阐明本发明的内容,但本发明的内容不仅仅局限于下面的实施例。 In order to better understand the present invention, the content of the present invention is further illustrated below in conjunction with the examples, but the content of the present invention is not limited to the following examples.
实施例1:Example 1:
本实施例提供一种改性陶瓷滤料,它可由下述方法制备: The present embodiment provides a modified ceramic filter material, which can be prepared by the following method:
1)预处理陶瓷滤料:将粒径为1.0-1.25mm的陶瓷滤料置于桶中,用自来水反复冲洗干净,用浓度为0.2mol/L的HCl溶液浸泡24h,然后用蒸馏水冲洗干净,直至冲洗水的pH值接近中性,再将陶瓷滤料置于托盘中在120℃干燥箱中烘干2h; 1) Pretreatment ceramic filter material: put the ceramic filter material with a particle size of 1.0-1.25mm in a bucket, rinse it repeatedly with tap water, soak it in HCl solution with a concentration of 0.2mol/L for 24 hours, and then rinse it with distilled water. Until the pH value of the rinse water is close to neutral, then place the ceramic filter material in a tray and dry it in a drying oven at 120°C for 2 hours;
2)配制改性溶液:在室温下取2.643x10-3mol环糊精,滴加DMF溶剂并搅拌至环糊精全部溶解,得到环糊精溶液;将所述环糊精溶液加入至反应器内,将反应器置于30-40℃的水浴中;将20.428x10-3mol高分子单体二苯基甲烷二异氰酸酯滴加至反应器中与环糊精溶液混合并搅拌,同时进行紫外光引发;其中,紫外光的功率为4KW,调整搅拌转速为120r/min,使充分接触反应;反应后,使用DMF溶剂洗涤所得到的固体产物,并使用蒸馏水再次洗涤,最后使用真空干燥,得到共聚物;取7.5g共聚物置于烧杯中并加入50mL蒸馏水,将烧杯放置在磁力搅拌器上搅拌得到悬浮物溶液,用浓度为10mol/L的NaOH控制溶液pH值为7.5; 2) Preparation of modification solution: Take 2.643x10 -3 mol cyclodextrin at room temperature, add DMF solvent dropwise and stir until the cyclodextrin is completely dissolved to obtain a cyclodextrin solution; add the cyclodextrin solution to the reactor Inside, place the reactor in a water bath at 30-40°C; add 20.428x10 -3 mol polymer diphenylmethane diisocyanate dropwise into the reactor, mix and stir with the cyclodextrin solution, and at the same time carry out ultraviolet light Initiation; wherein, the power of the ultraviolet light is 4KW, and the stirring speed is adjusted to be 120r/min, so as to fully contact the reaction; after the reaction, the obtained solid product is washed with DMF solvent, washed again with distilled water, and finally dried in vacuum to obtain a copolymerized Take 7.5g copolymer and place in beaker and add 50mL of distilled water, place the beaker on a magnetic stirrer and stir to obtain a suspension solution, and use NaOH with a concentration of 10mol/L to control the pH value of the solution to 7.5;
3)取步骤1)所得的陶瓷滤料于烧杯中,然后加入步骤2)所得的悬浮物溶液,所述悬浮物溶液的加入量以能封住陶瓷滤料为准,然后搅拌6h,将烧杯中物质转移入坩埚,放入烘箱中将水分蒸发干,然后移入马福炉中焙烧,焙烧温度定为650℃,焙烧时间定为2h,得到改性陶瓷滤料。 3) Take the ceramic filter material obtained in step 1) in a beaker, and then add the suspension solution obtained in step 2). The material in the medium was transferred into a crucible, put into an oven to evaporate the water to dryness, and then transferred to a muffle furnace for roasting at a temperature of 650°C and a roasting time of 2 hours to obtain a modified ceramic filter material.
实施例2: Embodiment 2 :
本实施例提供一种改性陶瓷滤料,它可由下述方法制备: The present embodiment provides a modified ceramic filter material, which can be prepared by the following method:
1)预处理陶瓷滤料:将粒径为1.0-1.25mm的陶瓷滤料置于桶中,用自来水反复冲洗干净,用浓度为0.1mol/L的HCl溶液浸泡24h,然后用蒸馏水冲洗干净,直至冲洗水的pH值接近中性,再将陶瓷滤料置于托盘中在110℃干燥箱中烘干2h; 1) Pretreatment of ceramic filter material: put the ceramic filter material with a particle size of 1.0-1.25mm in a bucket, rinse it repeatedly with tap water, soak it in HCl solution with a concentration of 0.1mol/L for 24 hours, and then rinse it with distilled water. Until the pH value of the rinse water is close to neutral, then place the ceramic filter material in a tray and dry it in a drying oven at 110°C for 2 hours;
2)配制改性溶液:取实施例1中步骤2)方法制备所得的共聚物5g置于烧杯中并加入50mL蒸馏水,将烧杯放置在磁力搅拌器上搅拌得到悬浮物溶液,用浓度为10mol/L的NaOH控制溶液pH值为7.0; 2) Preparation of modified solution: Take 5g of the copolymer prepared by the method of step 2) in Example 1, put it in a beaker, add 50mL of distilled water, place the beaker on a magnetic stirrer and stir to obtain a suspension solution, and use a concentration of 10mol/ L of NaOH control solution pH value is 7.0;
3)取步骤1)所得的陶瓷滤料于烧杯中,然后加入步骤2)所得的悬浮物溶液,所述悬浮物溶液的加入量以能封住陶瓷滤料为准,然后搅拌6h,将烧杯中物质转移入坩埚,放入烘箱中将水分蒸发干,然后移入马福炉中焙烧,焙烧温度定为550℃,焙烧时间定为2h,得到改性陶瓷滤料。 3) Take the ceramic filter material obtained in step 1) in a beaker, and then add the suspension solution obtained in step 2). The material in the medium was transferred into a crucible, put into an oven to evaporate the water to dryness, and then transferred to a muffle furnace for roasting, the roasting temperature was set at 550°C, and the roasting time was set at 2 hours to obtain a modified ceramic filter material.
在本实施例中,异氰酸酯选用六亚甲基二异氰酸酯。 In this embodiment, the isocyanate is selected from hexamethylene diisocyanate.
实施例3: Embodiment 3 :
本实施例提供一种改性陶瓷滤料,它可由下述方法制备: The present embodiment provides a modified ceramic filter material, which can be prepared by the following method:
1)预处理陶瓷滤料:将粒径为1.0-1.25mm的陶瓷滤料置于桶中,用自来水反复冲洗干净,用浓度为0.1mol/L的HCl溶液浸泡24h,然后用蒸馏水冲洗干净,直至冲洗水的pH值接近中性,再将陶瓷滤料置于托盘中在100℃干燥箱中烘干2h; 1) Pretreatment of ceramic filter material: put the ceramic filter material with a particle size of 1.0-1.25mm in a bucket, rinse it repeatedly with tap water, soak it in HCl solution with a concentration of 0.1mol/L for 24 hours, and then rinse it with distilled water. Until the pH value of the rinse water is close to neutral, then place the ceramic filter material in a tray and dry it in a drying oven at 100°C for 2 hours;
2)配制改性溶液:取实施例1中步骤2)方法制备所得的共聚物5g置于烧杯中并加入50mL蒸馏水,将烧杯放置在磁力搅拌器上搅拌得到悬浮物溶液,用浓度为10mol/L的NaOH控制溶液pH值为6.5; 2) Preparation of modified solution: Take 5g of the copolymer prepared by the method of step 2) in Example 1, put it in a beaker, add 50mL of distilled water, place the beaker on a magnetic stirrer and stir to obtain a suspension solution, and use a concentration of 10mol/ The NaOH control solution pH value of L is 6.5;
3)取步骤1)所得的陶瓷滤料于烧杯中,然后加入步骤2)所得的悬浮物溶液,所述悬浮物溶液的加入量以能封住陶瓷滤料为准,然后搅拌6h,将烧杯中物质转移入坩埚,放入烘箱中将水分蒸发干,然后移入马福炉中焙烧,焙烧温度定为450℃,焙烧时间定为2h,得到改性陶瓷滤料。 3) Take the ceramic filter material obtained in step 1) in a beaker, and then add the suspension solution obtained in step 2). The material in the medium was transferred into a crucible, put into an oven to evaporate the water to dryness, and then transferred to a muffle furnace for roasting at a temperature of 450°C and a roasting time of 2 hours to obtain a modified ceramic filter material.
在本实施例中,异氰酸酯选用甲苯二异氰酸酯。 In this embodiment, toluene diisocyanate is selected as the isocyanate.
根据以上实施例,选取实施例1-3条件下制备的改性陶瓷滤料,将得到的滤料用于研究含氯苯废水的处理效果,具体实验及结果如下: According to the above examples, the modified ceramic filter material prepared under the conditions of Examples 1-3 is selected, and the obtained filter material is used to study the treatment effect of chlorobenzene-containing wastewater. The specific experiments and results are as follows:
实验装置: experimental device:
采用直径为25mm,高1500mm的透明有机玻璃柱为模型滤柱。滤柱中采取改性陶瓷滤料粒径1.0-1.25mm,滤层厚度150-350mm,滤速2-8m/h。采用砾石作为承托层,从上到下粒径逐渐增大,总厚度100mm。 A transparent plexiglass column with a diameter of 25 mm and a height of 1500 mm is used as a model filter column. The modified ceramic filter material used in the filter column has a particle size of 1.0-1.25mm, a filter layer thickness of 150-350mm, and a filtration rate of 2-8m/h. Gravel is used as the supporting layer, and the particle size gradually increases from top to bottom, with a total thickness of 100mm.
原水的配制:取氯苯标样溶于蒸馏水中制备模拟废水。 Raw water preparation: Dissolve chlorobenzene standard sample in distilled water to prepare simulated wastewater.
(1)不同浓度氯苯废水的处理实验: (1) Treatment experiments of chlorobenzene wastewater with different concentrations:
取氯苯标样用蒸馏水配制成浓度为5mg/L、20mg/L、50mg/L的待处理水样各四份,分别编号为A、B。A水样采用的实验装置滤柱中滤料为改性前的陶瓷滤料,作为对比例,B采用本发明实施例2改性后的陶瓷滤料,实验装置滤柱中滤层厚度取350mm,滤速取4m/h,两水样分别经过滤柱过滤。过滤中尽量保持进、出水流量稳定。 Take the chlorobenzene standard sample and prepare four water samples with concentrations of 5mg/L, 20mg/L, and 50mg/L with distilled water, numbered A and B respectively. The filter material in the experimental device filter column that A water sample adopts is the ceramic filter material before modification, as a comparative example, B adopts the modified ceramic filter material of Example 2 of the present invention, and the thickness of the filter layer in the experimental device filter column is 350mm , the filtration rate is 4m/h, and the two water samples are filtered through the filter column respectively. Keep the flow of water in and out as stable as possible during filtration.
氯苯浓度为5mg/L时,氯苯去除结果见下表1: When the concentration of chlorobenzene is 5mg/L, the removal results of chlorobenzene are shown in the following table 1:
表1 Table 1
氯苯浓度为20mg/L时,氯苯去除结果见下表2: When the concentration of chlorobenzene is 20mg/L, the removal results of chlorobenzene are shown in the following table 2:
表2 Table 2
氯苯浓度为50mg/L时,氯苯去除结果见下表3: When the concentration of chlorobenzene is 50mg/L, the removal results of chlorobenzene are shown in the following table 3:
表3 table 3
由以上实验结果可以得出:本发明改性陶瓷滤料对于不同浓度的氯苯废水均有去除效果,且效果显著。相比于改性前的陶瓷滤料去除率有大幅提高,这是因为负载于陶瓷滤料表面的共聚物改性剂与陶瓷滤料协同作用,陶瓷滤料由于其自身孔洞繁密、孔隧深浅不一,高孔隙率往往得不到充分利用,单独作用时不能最大化发挥其吸附效果。改性后,共聚物改性剂能快速有效的吸附水中污染物质,即使负载在深邃孔洞中的共聚物也能以其强有力的吸附基团的作用,使污染物得以吸附去除。同时,陶瓷滤料的高孔隙率、高比表面积也为共聚物改性剂提供了栖身场所,两者协同互助共同吸附去除水中氯苯。 From the above experimental results, it can be concluded that the modified ceramic filter material of the present invention has a remarkable removal effect on chlorobenzene wastewater of different concentrations. Compared with the ceramic filter material before modification, the removal rate has been greatly improved. This is because the copolymer modifier loaded on the surface of the ceramic filter material works synergistically with the ceramic filter material. Not one, the high porosity is often not fully utilized, and its adsorption effect cannot be maximized when acting alone. After modification, the copolymer modifier can quickly and effectively adsorb pollutants in water. Even the copolymer loaded in deep pores can absorb and remove pollutants with its strong adsorption groups. At the same time, the high porosity and high specific surface area of the ceramic filter material also provide a shelter for the copolymer modifier, and the two cooperate to adsorb and remove chlorobenzene in water.
(2)不同滤层厚度时氯苯废水的处理实验: (2) Experiments on the treatment of chlorobenzene wastewater with different filter thicknesses:
取氯苯标样用蒸馏水配制成浓度为20mg/L的待处理水样四份,分别编号为E、F,设3组上述相同水样供后续实验。E水样采用的实验装置滤柱中滤料为改性前的陶瓷滤料,F采用本发明实施例2改性后的陶瓷滤料,实验装置滤柱中滤层厚度分别取150mm、250mm、350mm,滤速取4m/h,两水样分别经过滤柱过滤。过滤中尽量保持进、出水流量稳定。 The chlorobenzene standard sample was prepared with distilled water to prepare four water samples with a concentration of 20 mg/L, numbered E and F respectively, and three groups of the same water samples were set up for subsequent experiments. Filter material in the experimental device filter column that E water sample adopts is the ceramic filter material before modification, F adopts the ceramic filter material after the modification of the embodiment of the present invention 2, and the thickness of the filter layer in the experimental device filter column is respectively 150mm, 250mm, 350mm, the filtration rate is 4m/h, and the two water samples are filtered through the filter column respectively. Keep the flow of water in and out as stable as possible during filtration.
滤层厚度为150mm时,氯苯去除结果见下表4: When the thickness of the filter layer is 150mm, the removal results of chlorobenzene are shown in Table 4 below:
表4 Table 4
滤层厚度为250mm时,氯苯去除结果见下表5: When the thickness of the filter layer is 250mm, the removal results of chlorobenzene are shown in Table 5 below:
表5 table 5
滤层厚度为350mm,氯苯去除结果见下表6: The thickness of the filter layer is 350mm, and the removal results of chlorobenzene are shown in Table 6 below:
表6 Table 6
由以上实验结果可以得出:在一定的滤层厚度范围内,改性前与改性后的滤料对氯苯的去除均有一定的效果,相比而言,本发明改性陶瓷滤料较改性前去除率大幅提高,且随着滤层厚度的增大,氯苯去除率也随之增大。 From the above experimental results, it can be concluded that within a certain filter thickness range, the filter material before modification and after modification has a certain effect on the removal of p-chlorobenzene. In comparison, the modified ceramic filter material of the present invention Compared with that before modification, the removal rate is greatly improved, and with the increase of the thickness of the filter layer, the removal rate of chlorobenzene also increases.
(3)不同滤速时氯苯废水的处理实验: (3) Experiments on the treatment of chlorobenzene wastewater at different filtration rates:
取氯苯标样用蒸馏水配制成浓度为20mg/L的待处理水样两份,分别编号为G、H,设4组上述相同水样供后续实验。G水样采用的实验装置滤柱中滤料为改性前的陶瓷滤料,H采用实施例2改性后的陶瓷滤料,实验装置滤柱中滤层厚度取350mm,滤速分别取2m/h、4m/h、6m/h、8m/h,两水样分别经过滤柱过滤。过滤中尽量保持进、出水流量稳定。 The chlorobenzene standard sample was prepared with distilled water to prepare two water samples with a concentration of 20 mg/L, numbered G and H respectively, and 4 groups of the same water samples were set up for subsequent experiments. The filter material in the filter column of the experimental device adopted by G water sample is the ceramic filter material before modification, H adopts the modified ceramic filter material in Example 2, the thickness of the filter layer in the filter column of the experimental device is 350mm, and the filtration rate is 2m respectively /h, 4m/h, 6m/h, 8m/h, the two water samples are filtered through the filter column respectively. Keep the flow of water in and out as stable as possible during filtration.
滤速为2m/h时,氯苯去除结果见下表7: When the filtration rate is 2m/h, the removal results of chlorobenzene are shown in Table 7 below:
表7 Table 7
滤速为4m/h时,氯苯去除结果见下表8: When the filtration rate is 4m/h, the removal results of chlorobenzene are shown in Table 8 below:
表8 Table 8
滤速为6m/h时,氯苯去除结果见下表9: When the filtration rate is 6m/h, the removal results of chlorobenzene are shown in Table 9 below:
表9 Table 9
滤速为8m/h时,氯苯去除结果见下表10: When the filtration rate is 8m/h, the removal results of chlorobenzene are shown in Table 10 below:
表10 Table 10
由以上实验结果可以得出:在一定的滤速范围内,改性前与改性后的滤料对氯苯的去除均有一定的效果,相比而言,改性后去除率大幅提高。另外,两种滤料随着滤速的增加,去除率均有降低,但相比于改性前滤料,本发明改性陶瓷滤料去除率降低不甚明显。综合考虑总体技术经济的因素,在实际应用中可选用4m/h滤速。 From the above experimental results, it can be concluded that within a certain filtration rate range, both the pre-modified and the modified filter materials have certain effects on the removal of p-chlorobenzene. In comparison, the removal rate after modification is greatly improved. In addition, with the increase of the filtration rate, the removal rate of the two filter materials decreases, but compared with the filter material before modification, the reduction of the removal rate of the modified ceramic filter material of the present invention is not obvious. Considering the overall technical and economic factors comprehensively, 4m/h filtration rate can be selected in practical application.
选取实施例1和实施例3条件下制备的改性陶瓷滤料,参考上述实验,选取氯苯浓度为20mg/L,滤层厚度为350mm,滤速为4m/h,探究含氯苯废水的处理效果,氯苯去除结果见下表11: Select the modified ceramic filter material prepared under the conditions of Example 1 and Example 3, refer to the above experiment, choose the concentration of chlorobenzene to be 20mg/L, the thickness of the filter layer is 350mm, and the filtration rate is 4m/h to explore the chlorobenzene-containing wastewater. Treatment effect, chlorobenzene removal result is shown in the following table 11:
表11 Table 11
本发明实施例中所选用的陶瓷滤料为根据中国专利申请号为200810197939.6,发明名称为“利用镁渣制备环保陶瓷滤料的方法”制备得到的陶瓷滤料。可以理解的是,其它市售的陶瓷滤料也可以为本发明所用。 The ceramic filter material used in the embodiment of the present invention is a ceramic filter material prepared according to the Chinese patent application number 200810197939.6, and the title of the invention is "Method for Preparing Environmentally Friendly Ceramic Filter Material Using Magnesium Slag". It can be understood that other commercially available ceramic filter materials can also be used in the present invention.
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《二醋酸纤维素与β-环糊精接枝共聚物膜的制备与表征》;朱虹;《Chemical Reaction Engineering and Technology》;20120115;第27卷(第27期);第245-251页 * |
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