CN113044949B - Sodium Persulfate Sustained Release Agent Suitable for Catalytic Oxidative Degradation of Antibiotics and Its Preparation and Application - Google Patents
Sodium Persulfate Sustained Release Agent Suitable for Catalytic Oxidative Degradation of Antibiotics and Its Preparation and Application Download PDFInfo
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Abstract
Description
技术领域technical field
本发明涉及土壤和地下水修复技术领域,具体涉及一种适用于催化氧化降解抗生素的过硫酸钠(Na2S2O8)缓释剂及其制备和应用。The invention relates to the technical field of soil and groundwater remediation, in particular to a sodium persulfate (Na 2 S 2 O 8 ) slow-release agent suitable for catalyzing and oxidatively degrading antibiotics and its preparation and application.
背景技术Background technique
伴随着经济社会的不断发展,我国的土壤和地下水环境在近年来受到严重的污染威胁。尤其地下水由于复杂的地质特性,土壤的包覆作用,地下水的动力学作用和微生物的协同作用都能够让污染物在此隐蔽起来,这就使得处理地下水中的污染物质变得格外棘手。如果仅依靠自然降解,那么这些有机污染物达到无害化水平需要几百到几千年,因此,有必要开发一种切实有效的治理方式,解决土壤及地下水污染。With the continuous development of economy and society, my country's soil and groundwater environment has been threatened by serious pollution in recent years. In particular, the complex geological characteristics of groundwater, the coating of soil, the dynamic action of groundwater and the synergy of microorganisms can hide pollutants here, which makes it particularly difficult to deal with pollutants in groundwater. If only relying on natural degradation, it will take hundreds to thousands of years for these organic pollutants to reach harmless level. Therefore, it is necessary to develop a practical and effective treatment method to solve soil and groundwater pollution.
近年来,越来越多的抗生素被排放到土壤和地下水中,如何解决好抗生素污染受到了广大学者们的关注。以四环素为代表的抗生素污染物由于其顽固的特性,复杂的迁移特点等原因,使得研究者往往对其无从下手,土壤会成为污染物的庇护所,修复剂不能够集中处理污染物;不仅如此,四环素还会利用土壤包覆作用等的特性,不停向地下水中释放污染,造成持续污染作用。所以,简单的治理方式往往不能很好地解决这一难题,解决好这一难题成为了众多研究学者的目标。In recent years, more and more antibiotics have been discharged into soil and groundwater, and how to solve antibiotic pollution has attracted the attention of scholars. Antibiotic pollutants represented by tetracycline, due to their stubborn characteristics and complex migration characteristics, make researchers often unable to deal with them. , Tetracycline will also use the characteristics of soil coating and other characteristics to continuously release pollution into groundwater, causing continuous pollution. Therefore, simple governance methods often cannot solve this problem well, and solving this problem has become the goal of many researchers.
化学氧化型缓释剂就在这种情况下应运而生,缓释剂对于普通的修复方式来说,能够对污染物进行精确的靶向治理,具有较长的持续释放时间,并且可以有效治理那些从低渗透含水层中反向释放出来的污染物,不仅如此,还能控制反应物量的释放速度。化学氧化型缓释剂有望处理土壤及地下水中的四环素。Chemical oxidation slow-release agents came into being in this situation. For ordinary repair methods, slow-release agents can precisely target pollutants, have a long sustained release time, and can effectively treat pollutants. Those contaminants that are back-released from low-permeability aquifers, not only that, but also control the rate at which the amount of reactant is released. Chemical oxidative slow-release agents are expected to treat tetracycline in soil and groundwater.
杨苑等人研究了过硫酸钠-石蜡-硅砂缓释材料的释放性能及其对2,4-二硝基甲苯的降解效果,有望用于原位化学氧化修复土壤和地下水(《过硫酸钠缓释材料的释放性能及其对2,4-二硝基甲苯的降解效果》,《环境科学研究》,2020年3月,第33卷第3期)。Yang Yuan et al. studied the release properties of sodium persulfate-paraffin-silica sand sustained-release material and its degradation effect on 2,4-dinitrotoluene, which is expected to be used for in-situ chemical oxidation remediation of soil and groundwater ("Sodium Persulfate"). Release properties of sustained-release materials and their degradation effect on 2,4-dinitrotoluene", "Environmental Science Research", March 2020, Vol. 33, No. 3).
张丽娜硕士学位论文《四氧化三铁激活过硫酸钠降解地下水中有机污染物的研究》报道了二氧化锰等过渡金属氧化物为激活剂激活过硫酸钠降解1,2-二氯丙烷的效果,但并未对二氧化锰进行深入研究。Zhang Lina's master's thesis "Research on the Activation of Sodium Persulfate by Ferric Oxide to Degrade Organic Pollutants in Groundwater" reported the effect of manganese dioxide and other transition metal oxides as activators to activate sodium persulfate to degrade 1,2-dichloropropane. But manganese dioxide has not been studied in depth.
发明内容SUMMARY OF THE INVENTION
针对本领域存在的不足之处,本发明提供了一种适用于催化氧化降解抗生素的过硫酸钠缓释剂,以过硫酸钠为主要氧化剂,有序介孔氧化锰为催化剂,两者协同可高效催化氧化降解四环素等抗生素。此外,本发明以石蜡为载体,同时加入石英砂,增强渗透性和吸附性。所述的过硫酸钠缓释剂包覆效果好、释放速率低、有良好渗透性和吸附性,具有良好的氧化降解特性,特别适用于修复抗生素污染物污染的土壤和地下水。In view of the deficiencies in the art, the present invention provides a sodium persulfate slow-release agent suitable for catalyzing and oxidatively degrading antibiotics. The sodium persulfate is used as the main oxidant and the ordered mesoporous manganese oxide is used as the catalyst. Efficiently catalyze the oxidative degradation of tetracycline and other antibiotics. In addition, the present invention uses paraffin as a carrier and adds quartz sand at the same time to enhance permeability and adsorption. The sodium persulfate slow-release agent has good coating effect, low release rate, good permeability and adsorption, and good oxidative degradation characteristics, and is especially suitable for repairing soil and groundwater polluted by antibiotic pollutants.
一种适用于催化氧化降解抗生素的过硫酸钠缓释剂,以原料总质量为100%计,原料组成包括:A sodium persulfate sustained-release agent suitable for catalyzing and oxidatively degrading antibiotics, calculated on the basis of the total mass of raw materials as 100%, the raw material composition includes:
所述有序介孔氧化锰通过硬模板法制备得到,模板剂采用SBA-15。The ordered mesoporous manganese oxide is prepared by a hard template method, and the template agent is SBA-15.
研究发现,普通商用二氧化锰作为催化剂与过硫酸钠联用用于处理四环素等抗生素时,并不能产生很好地催化氧化效果。而采用本发明所述的以SBA-15为模板剂、通过硬模板法制备得到的有序介孔氧化锰为催化剂与过硫酸钠联用用于处理四环素等抗生素时,两者协同作用表现出明显更优异的催化氧化降解四环素等抗生素性能,说明本发明的有序介孔氧化锰对过硫酸钠具有优异的催化作用,可最大程度地发挥出过硫酸钠的氧化性能。The study found that when ordinary commercial manganese dioxide was used as a catalyst in combination with sodium persulfate to treat antibiotics such as tetracycline, it could not produce a good catalytic oxidation effect. When the ordered mesoporous manganese oxide prepared by the hard template method using SBA-15 as a template agent of the present invention is used as a catalyst in combination with sodium persulfate to treat antibiotics such as tetracycline, the synergistic effect of the two shows a synergistic effect. The significantly better catalytic oxidation degradation performance of antibiotics such as tetracycline indicates that the ordered mesoporous manganese oxide of the present invention has an excellent catalytic effect on sodium persulfate, and can maximize the oxidation performance of sodium persulfate.
为了更好地实现催化功能,优选地,所述有序介孔氧化锰为β-MnO2晶型结构,含有Mn4+和Mn3+,比表面积不小于80m2/g。同时具有Mn4+、Mn3+这两种可互相转化的价态的有序介孔氧化锰具有更佳的催化性能以及电子转移和传递能力。In order to better realize the catalytic function, preferably, the ordered mesoporous manganese oxide has a β-MnO 2 crystal structure, contains Mn 4+ and Mn 3+ , and has a specific surface area of not less than 80 m 2 /g. The ordered mesoporous manganese oxide with two interconvertible valence states of Mn 4+ and Mn 3+ has better catalytic performance and electron transfer and transfer ability.
所述硬模板法优选采用严凯鑫等人于2020年8月在《环境科学学报》第40卷第8期发表的《纳米刻蚀法制备氧化锰介孔材料及其降解高含盐废水中罗丹明B》中所描述的制备氧化锰有序介孔材料的方法。The hard template method preferably adopts the "Nano-etching method to prepare manganese oxide mesoporous materials and their degradation of rhodamine in high-salt wastewater" published by Yan Kaixin et al. The method for preparing manganese oxide ordered mesoporous materials described in "B".
具体地,所述硬模板法优选包括步骤:Specifically, the hard template method preferably comprises the steps:
(I)将硝酸锰水溶液加入到SBA-15的无水乙醇悬浮液中,搅拌充分吸附后加入氨水调节反应体系pH至10.5~11.5,继续搅拌10~20min后离心分离,洗涤固体产物直至中性,常温干燥后在350~450℃煅烧3~5h,得到煅烧产物;(1) the manganese nitrate aqueous solution is added in the dehydrated alcohol suspension of SBA-15, after stirring and fully adsorbing, add ammonia water to adjust the pH of the reaction system to 10.5~11.5, continue to stir after 10~20min centrifugation, wash the solid product until neutral , calcined at 350~450℃ for 3~5h after drying at room temperature to obtain a calcined product;
(II)用所述煅烧产物代替SBA-15,重复步骤(I),如此共进行1~3次迭代,得到复合产物;(II) replacing SBA-15 with the calcined product, repeating step (I), and performing 1 to 3 iterations in this way to obtain a composite product;
(III)将所述复合产物均匀分散于氢氧化钠溶液中,加热煮沸,回流条件下反应去除SBA-15,反应结束后离心分离,洗涤固体沉淀直至中性,55~65℃真空干燥即得所述有序介孔氧化锰。(III) The composite product is uniformly dispersed in the sodium hydroxide solution, heated and boiled, reacted to remove SBA-15 under reflux conditions, centrifuged after the reaction, washed the solid precipitation until neutral, and vacuum-dried at 55~65 ℃ to obtain The ordered mesoporous manganese oxide.
上述硬模板法制备得到的有序介孔氧化锰的有序度和结晶度高,有良好的吸附和催化能力,尤其对过硫酸钠氧化四环素等抗生素的过程具有极强的催化能力,并且循环使用稳定性强。The ordered mesoporous manganese oxide prepared by the above hard template method has high degree of order and high crystallinity, and has good adsorption and catalytic ability, especially for the process of sodium persulfate oxidation of tetracycline and other antibiotics. Strong stability in use.
作为优选,所述过硫酸钠和有序介孔氧化锰的质量比为5~10:1,进一步优选为5~8:1。有序介孔氧化锰的添加量和催化能力成正相关,但当催化剂添加量超过一定比例后,催化剂添加量再增多,其对催化反应促进作用的提升程度会有所减弱。Preferably, the mass ratio of the sodium persulfate to the ordered mesoporous manganese oxide is 5-10:1, more preferably 5-8:1. The addition amount of ordered mesoporous manganese oxide is positively correlated with the catalytic ability, but when the catalyst addition amount exceeds a certain proportion, the catalyst addition amount increases again, and its promotion effect on the catalytic reaction will be weakened.
本发明的过硫酸钠缓释剂选用石蜡、石英砂作为混合载体,其中:石蜡具有很好的粘合性,不溶于水,为环保材料;石英砂具有良好的渗透性,为绿色环保材料。该混合载体增加了缓释剂的包覆效果、渗透性和吸附性。The sodium persulfate slow-release agent of the present invention selects paraffin and quartz sand as mixed carriers, wherein: paraffin has good adhesion, is insoluble in water, and is an environmental protection material; quartz sand has good permeability and is a green environmental protection material. The mixed carrier increases the coating effect, permeability and adsorption of the sustained release agent.
本发明还提供了所述的过硫酸钠缓释剂的制备方法,包括步骤:The present invention also provides the preparation method of described sodium persulfate sustained-release agent, comprising the steps:
(1)将石蜡加入无水乙醇中,加热至60~80℃,待石蜡完全融化后,在搅拌下向其中依次加入表面活性剂、石英砂、有序介孔氧化锰和过硫酸钠;(1) adding paraffin into absolute ethanol, heating to 60~80 ℃, after the paraffin is completely melted, adding surfactant, quartz sand, ordered mesoporous manganese oxide and sodium persulfate to it under stirring;
(2)将步骤(1)得到的熔融态材料冷却即得所述过硫酸钠缓释剂。(2) cooling the molten material obtained in step (1) to obtain the sodium persulfate sustained-release agent.
由于石蜡的熔化温度范围是58~60℃,所以步骤(1)中,石蜡溶解时控制体系温度为60~80℃,可使石蜡完全融化。作为优选,步骤(1)中加热至70~75℃,更有利于步骤(2)中熔融态材料的转移,便于后续冷却。Since the melting temperature of the paraffin wax is in the range of 58-60° C., in step (1), the temperature of the system is controlled to be 60-80° C. when the paraffin wax is dissolved, so that the paraffin wax can be completely melted. Preferably, heating to 70-75° C. in step (1) is more conducive to the transfer of molten material in step (2) and facilitates subsequent cooling.
步骤(1)中,所述表面活性剂包括司盘-80和分子量为4000的聚乙二醇,起到乳化作用。所述司盘-80和聚乙二醇的质量比优选为0.01~0.2:1。所述无水乙醇和聚乙二醇的质量比优选为1~20:1。聚乙二醇还可起到溶解助剂的作用,辅助石蜡溶解。In step (1), the surfactant includes Span-80 and polyethylene glycol with a molecular weight of 4000, which plays an emulsifying effect. The mass ratio of Span-80 and polyethylene glycol is preferably 0.01-0.2:1. The mass ratio of the absolute ethanol and polyethylene glycol is preferably 1-20:1. Polyethylene glycol can also act as a dissolving aid to assist in dissolving paraffin.
作为优选,步骤(1)中,所述搅拌的转速为100~200rpm,搅拌总时间为5~30min。Preferably, in step (1), the rotational speed of the stirring is 100-200 rpm, and the total stirring time is 5-30 min.
熔融的缓释剂在成型前处于流动状态,一旦降温石蜡将会较快凝结,定型时间较少。步骤(2)中,为了使冷却得到的过硫酸钠缓释剂具有固定的形状尺寸,可将步骤(1)得到的熔融态材料倒入模具中进行冷却,得到所述过硫酸钠缓释剂。The molten slow-release agent is in a flowing state before molding, and once the temperature is lowered, the paraffin will condense faster, and the setting time will be less. In step (2), in order to make the sodium persulfate slow-release agent obtained by cooling have a fixed shape and size, the molten material obtained in step (1) can be poured into the mold for cooling to obtain the sodium persulfate slow-release agent. .
所述模具的具体尺寸可以为1.0cm×1.0cm×1.0cm。The specific size of the mold may be 1.0cm×1.0cm×1.0cm.
上述制备方法的原理在于:基于控制释放技术和微胶囊技术,利用熔化冷凝分散法将氧化剂过硫酸钠和催化剂有序介孔氧化锰均匀分散在以石蜡、石英砂等为载体的熔融态液体中,加入无水乙醇、聚乙二醇、司盘-80等试剂辅助载体、氧化剂和催化剂混合均匀稳定,最后趁热倒入模具,冷却干燥后形成固体颗粒,以达到缓释的目的。The principle of the above preparation method is: based on the controlled release technology and the microcapsule technology, the oxidant sodium persulfate and the catalyst ordered mesoporous manganese oxide are uniformly dispersed in the molten liquid with paraffin, quartz sand, etc. as the carrier by the melting condensation dispersion method. , adding anhydrous ethanol, polyethylene glycol, Span-80 and other reagents to assist the carrier, oxidant and catalyst to mix evenly and stably, and finally pour it into the mold while hot, cool and dry to form solid particles to achieve the purpose of slow release.
本发明还提供了所述的过硫酸钠缓释剂在修复受抗生素污染的土壤和地下水中的应用。The invention also provides the application of the sodium persulfate slow-release agent in repairing soil and groundwater contaminated by antibiotics.
优选地,所述抗生素为四环素(Tetracycline,简称TC)。研究发现,四环素等抗生素非常稳定,单一过硫酸钠无法直接氧化这些抗生素,必须要有特定催化剂的辅助催化作用方可实现对四环素等抗生素的有效氧化降解。Preferably, the antibiotic is Tetracycline (TC for short). Studies have found that antibiotics such as tetracycline are very stable, and a single sodium persulfate cannot directly oxidize these antibiotics. The effective oxidative degradation of antibiotics such as tetracycline can only be achieved by the auxiliary catalytic action of a specific catalyst.
本发明与现有技术相比,主要优点包括:Compared with the prior art, the main advantages of the present invention include:
1)本发明的过硫酸钠缓释剂以过硫酸钠为主要氧化剂,有序介孔氧化锰为催化剂,石蜡为载体,同时加入石英砂,增强渗透性和吸附性。所述有序介孔氧化锰具有较大的比表面积,较高的有序度和结晶度,以及具有良好的循环利用性能,对催化过硫酸钠氧化四环素等抗生素具有独特的优异能力;所述的过硫酸钠缓释剂包覆效果好、释放速率低、有良好渗透性和吸附性,在所述有序介孔氧化锰的协同催化作用下,氧化降解性能显著提升,可用于修复四环素等抗生素污染物污染的土壤和地下水。1) The sodium persulfate slow-release agent of the present invention uses sodium persulfate as the main oxidant, ordered mesoporous manganese oxide as the catalyst, paraffin as the carrier, and adds quartz sand at the same time to enhance permeability and adsorption. The ordered mesoporous manganese oxide has large specific surface area, high order degree and crystallinity, and has good recycling performance, and has a unique and excellent ability to catalyze the oxidation of tetracycline and other antibiotics by sodium persulfate; The sodium persulfate sustained-release agent has good coating effect, low release rate, good permeability and adsorption, and under the synergistic catalysis of the ordered mesoporous manganese oxide, the oxidative degradation performance is significantly improved, which can be used to repair tetracycline, etc. Soil and groundwater contaminated by antibiotic contaminants.
2)本发明的过硫酸钠缓释剂的制备方法基于控制释放技术和微胶囊技术,利用熔化冷凝分散法将氧化剂过硫酸钠和催化剂有序介孔氧化锰均匀分散在以石蜡、石英砂等为载体的熔融态液体中,加入无水乙醇、聚乙二醇、司盘-80等试剂辅助载体和氧化剂混合均匀稳定,最后趁热倒入模具,冷却干燥后形成固体颗粒,以达到缓释的目的。2) The preparation method of the sodium persulfate sustained-release agent of the present invention is based on the controlled release technology and the microcapsule technology, and the oxidant sodium persulfate and the catalyst ordered mesoporous manganese oxide are uniformly dispersed in paraffin, quartz sand, etc. In the molten liquid as the carrier, add anhydrous ethanol, polyethylene glycol, Span-80 and other reagents to assist the carrier and the oxidant to mix evenly and stably, and finally pour it into the mold while still hot, and cool and dry to form solid particles to achieve sustained release. the goal of.
3)本发明的过硫酸钠缓释剂在水中释放速率明显降低,渗透性增强,吸附性和氧化性增强;同时,其释放周期变长,缓释剂释放速度较为稳定,尤其对TC污染的土壤、废水具有良好的处理效果。3) The release rate of the sodium persulfate sustained-release agent of the present invention in water is significantly reduced, the permeability is enhanced, and the adsorption and oxidizing properties are enhanced; meanwhile, its release period becomes longer, and the release rate of the sustained-release agent is relatively stable, especially for TC polluted water. Soil and wastewater have good treatment effect.
附图说明Description of drawings
图1为实施例3的缓释剂的实物照片;Fig. 1 is the real photo of the slow-release agent of embodiment 3;
图2为实施例3的缓释剂静态释放过硫酸钠浓度随时间变化图;Fig. 2 is the time variation diagram of the sustained-release agent static release sodium persulfate concentration of embodiment 3;
图3为实施例3的缓释剂静态修复实验中四环素相对浓度随时间变化图;3 is a graph showing the relative concentration of tetracycline in the static repair experiment of the slow-release agent of Example 3 over time;
图4为实施例3的动态释放实验中的过硫酸钠浓度随时间变化图,图中CRM标签代表实施例3的缓释剂;Fig. 4 is a graph showing the variation of sodium persulfate concentration with time in the dynamic release experiment of Example 3, in which CRM label represents the sustained-release agent of Example 3;
图5为实施例3的动态修复实验中的四环素相对浓度随时间变化图,图中CRM标签代表实施例3的缓释剂;Fig. 5 is a graph of the relative concentration of tetracycline in the dynamic repair experiment of Example 3 over time, and the CRM label in the figure represents the sustained-release agent of Example 3;
图6为测试例1的不同催化剂对四环素降解的相对浓度变化图;Fig. 6 is the relative concentration change diagram of the different catalysts of Test Example 1 to the degradation of tetracycline;
图7为测试例2的不同有序介孔氧化锰添加量的缓释剂静态修复六小时四环素相对浓度变化图;Fig. 7 is the change diagram of the relative concentration of tetracycline in six hours of static repair of slow-release agents with different addition amounts of ordered mesoporous manganese oxide of Test Example 2;
图8为测试例3的不同蜡砂比的缓释剂静态释放六小时过硫酸钠浓度变化图;Fig. 8 is that the slow-release agent of different wax-sand ratios of Test Example 3 is statically released six hours sodium persulfate concentration variation diagram;
图9为测试例4的不同过硫酸钠添加量的缓释剂静态释放六小时过硫酸钠浓度变化图。FIG. 9 is a graph showing the concentration change of sodium persulfate in six hours of static release of slow-release agents with different addition amounts of sodium persulfate in Test Example 4.
具体实施方式Detailed ways
下面结合附图及具体实施例,进一步阐述本发明。应理解,这些实施例仅用于说明本发明而不用于限制本发明的范围。下列实施例中未注明具体条件的操作方法,通常按照常规条件,或按照制造厂商所建议的条件。The present invention will be further described below with reference to the accompanying drawings and specific embodiments. It should be understood that these examples are only used to illustrate the present invention and not to limit the scope of the present invention. The operation method without specifying the specific conditions in the following examples is usually in accordance with the conventional conditions, or in accordance with the conditions suggested by the manufacturer.
具体实施方式中有序介孔氧化锰的制备方法:The preparation method of ordered mesoporous manganese oxide in the specific embodiment:
(I)将4mL浓度为50wt%的硝酸锰水溶液加入到含3g SBA-15的50mL无水乙醇悬浮液中,0℃搅拌4h充分吸附后加入氨水调节反应体系pH至11,继续搅拌15min后离心分离,洗涤固体产物直至中性,常温干燥后在400℃煅烧4h,得到煅烧产物;(1) 4mL concentration is that the manganese nitrate aqueous solution of 50wt% is added in the 50mL dehydrated alcohol suspension containing 3g SBA-15, after 0 ℃ of stirring 4h fully adsorb, add ammonia water to adjust the pH of the reaction system to 11, continue to stir after 15min centrifugal Separation, washing the solid product until neutral, drying at room temperature and then calcining at 400 °C for 4 hours to obtain a calcined product;
(II)用所述煅烧产物代替SBA-15,重复步骤(I),得到复合产物;(II) replacing SBA-15 with the calcined product, repeating step (I) to obtain a composite product;
(III)将所述复合产物均匀分散于200mL 2mol/L的氢氧化钠溶液中,加热煮沸,回流条件下反应去除SBA-15,反应结束后离心分离,洗涤固体沉淀直至中性,60℃真空干燥24h即得所述有序介孔氧化锰。(III) The composite product is uniformly dispersed in the sodium hydroxide solution of 200mL 2mol/L, heated and boiled, and SBA-15 is removed by reaction under reflux conditions, and the reaction is centrifuged after finishing, and the solid precipitation is washed until neutral, 60 ° C of vacuum The ordered mesoporous manganese oxide was obtained after drying for 24 hours.
实施例1Example 1
使用商用二氧化锰(国药集团化学试剂有限公司,分析纯)为催化剂,催化过硫酸钠降解四环素,控制四环素的初始浓度为20mg/L,催化剂=0.1g/L,Na2S2O8=2mmol/L。Use commercial manganese dioxide (Sinopharm Chemical Reagent Co., Ltd., analytical grade) as a catalyst to catalyze the degradation of tetracycline by sodium persulfate, and control the initial concentration of tetracycline to be 20 mg/L, catalyst = 0.1 g/L, Na 2 S 2 O 8 = 2mmol/L.
实施例2Example 2
使用有序介孔氧化锰为催化剂,催化过硫酸钠降解四环素,采用与实施例1相同的测试条件,控制四环素的初始浓度为20mg/L,催化剂=0.1g/L,Na2S2O8=2mmol/L。Using ordered mesoporous manganese oxide as a catalyst to catalyze the degradation of tetracycline by sodium persulfate, using the same test conditions as in Example 1, controlling the initial concentration of tetracycline to be 20mg/L, catalyst=0.1g/L, Na 2 S 2 O 8 =2mmol/L.
实施例3Example 3
使用缓释剂为过硫酸钠、石蜡、石英砂和介孔二氧化锰质量比为4:12:12:0.5的混合吸附缓释剂。The slow-release agent was a mixed adsorption slow-release agent with a mass ratio of sodium persulfate, paraffin, quartz sand and mesoporous manganese dioxide of 4:12:12:0.5.
(1)缓释剂的制备(1) Preparation of sustained release agent
基于微胶囊技术,采用熔化冷凝分散法,制备缓释剂。取12g的石蜡于锥形瓶中,加入20mL无水乙醇,水浴加热至75℃;待石蜡完全融化,加入1g聚乙二醇-4000和2滴司盘-80,充分搅拌;按4:12:12:0.5的质量比例依次加入12g石英砂、0.5g有序介孔氧化锰和4g过硫酸钠粉末,搅拌使其均匀分散;趁热倒入准备好的规格为1.0cm×1.0cm×1.0cm的模具中;经过冷却干燥后即可得到正方体型固体新型过硫酸钠缓释剂。Based on the microcapsule technology, the slow-release agent is prepared by melting condensation dispersion method. Take 12g of paraffin into a conical flask, add 20mL of absolute ethanol, and heat to 75°C in a water bath; when the paraffin is completely melted, add 1g of polyethylene glycol-4000 and 2 drops of Span-80, and stir well; press 4:12 Add 12g quartz sand, 0.5g ordered mesoporous manganese oxide and 4g sodium persulfate powder in sequence in a mass ratio of 12:0.5, and stir to disperse evenly; cm; after cooling and drying, a cube-shaped solid new sodium persulfate sustained-release agent can be obtained.
图1为过硫酸钠、石蜡、石英砂和介孔二氧化锰质量比为4:12:12:0.5的缓释剂的实物照片。Figure 1 is a real photo of a sustained-release agent with a mass ratio of sodium persulfate, paraffin, quartz sand and mesoporous manganese dioxide of 4:12:12:0.5.
(2)缓释剂静态释放(2) Static release of sustained release agent
静态释放实验的原理是通过让不同缓释剂处于相同的液体环境下(水环境或有机溶液环境),让缓释剂中的氧化剂过硫酸钠释放,但不发生反应。在一定的时间内,设定时间点进行取样,用紫外分光光度仪测定不同时间的过硫酸钠浓度。The principle of the static release experiment is to release the oxidant sodium persulfate in the slow-release agent by placing different sustained-release agents in the same liquid environment (water environment or organic solution environment), but no reaction occurs. In a certain period of time, set time points for sampling, and measure the concentration of sodium persulfate at different times with an ultraviolet spectrophotometer.
取2.0g左右的固体缓释剂置于250mL的锥形瓶中;加入250mL水,开始计时;分别定时定量取1mL样品、1mL KI溶液、1mL NaHCO3溶液置于10mL比色管中,定容至10mL,记录标号(加空白样),手动摇匀15min;使用分光光度仪在352nm处测定过硫酸钠吸光度;计算其浓度,绘制折线图。缓释剂静态释放过硫酸钠浓度随时间变化如图2所示。Take about 2.0g of solid slow-release agent and place it in a 250mL conical flask; add 250mL of water and start timing; quantitatively take 1mL of sample, 1mL of KI solution, and 1mL of NaHCO3 solution in a 10mL colorimetric tube at regular intervals, and set the volume to constant volume. To 10mL, record the label (add blank sample), shake manually for 15min; use a spectrophotometer to measure the absorbance of sodium persulfate at 352nm; calculate its concentration and draw a line graph. Figure 2 shows the time-dependent change of the sodium persulfate concentration in the static release of the sustained-release agent.
(3)缓释剂静态修复(3) Static repair of slow release agent
模拟静态修复实验,选取的是具有代表性的抗生素污染物四环素。本实验就选用过硫酸钠来处理四环素微污染的模拟地下水,进行定时取样测量。有序介孔氧化锰催化过硫酸钠氧化四环素的处理效果较好。To simulate static repair experiments, a representative antibiotic pollutant, tetracycline, was selected. In this experiment, sodium persulfate was used to treat the simulated groundwater that was slightly polluted by tetracycline, and sampling measurements were carried out at regular intervals. Ordered mesoporous manganese oxide catalyzed the oxidation of tetracycline by sodium persulfate with better treatment effect.
配制低浓度四环素,充当污染水;取2g待测定缓释剂置于反应器中,加入100mL污染水,四环素含量为10mg/L;每隔一定时间取样一次,每次取5mL;用紫外分光光度法在352nm处测定样品中四环素浓度,并绘制浓度随时间变化曲线,结果如图3所示。Prepare low-concentration tetracycline to act as polluted water; take 2g of the slow-release agent to be measured and place it in the reactor, add 100mL of polluted water, and the tetracycline content is 10mg/L; take samples at regular intervals, 5mL each time; use UV spectrophotometry The concentration of tetracycline in the sample was measured at 352 nm by the method, and the curve of the concentration change with time was drawn. The results are shown in Figure 3.
(4)动态释放及修复(4) Dynamic release and repair
动态实验主要是模拟地下水的介质环境、流速,进行一维砂柱实验。在这种情况下,用混合吸附缓释剂对污染地下水进行修复,观察其修复效果。本实验在一维砂柱中进行。使用缓释剂为过硫酸钠、石蜡、石英砂和介孔二氧化锰质量比为4:12:12:0.5的混合吸附缓释剂。The dynamic experiment is mainly to simulate the medium environment and flow velocity of groundwater, and conduct one-dimensional sand column experiments. In this case, the contaminated groundwater was rehabilitated with the mixed adsorption slow-release agent, and the remediation effect was observed. This experiment was performed in a one-dimensional sand column. The slow-release agent was a mixed adsorption slow-release agent with a mass ratio of sodium persulfate, paraffin, quartz sand and mesoporous manganese dioxide of 4:12:12:0.5.
模拟地下水的介质环境、流速,进行一维砂柱实验。实验参数模拟地下水环境设置。实验柱介质的渗透系数为1.39×10-2cm/s;水流速度设置为2mL/min;实验柱的直径为R=5.0cm;实验柱长度为L=20cm,其中缓释剂占比长度为l1=3.0cm、前部缓冲介质占比l2=1.0cm、实际介质占比l3=15.0cm、后部缓冲介质占比l4=1.0cm。Simulate the medium environment and flow rate of groundwater, and conduct one-dimensional sand column experiments. The experimental parameters simulate the groundwater environment settings. The permeability coefficient of the experimental column medium is 1.39×10 -2 cm/s; the water flow rate is set to 2mL/min; the diameter of the experimental column is R=5.0cm; the length of the experimental column is L=20cm, and the proportion of the slow-release agent is l 1 =3.0cm, front buffer medium proportion l 2 =1.0cm, actual medium proportion l 3 =15.0cm, rear buffer medium proportion l 4 =1.0cm.
填充一维砂柱,并让一维砂柱内水(或污染水)饱和(200mL);在一维砂柱进水口处放2g过硫酸钠缓释剂;连接一维砂柱、水槽和蠕动泵;启动蠕动泵;以2.0mL/min的流速,泵入水;启动蠕动泵后定期取样,测定每次水样的过硫酸钠浓度(或四环素浓度);绘制过硫酸钠浓度(或四环素浓度)曲线。Fill the one-dimensional sand column and saturate the water (or polluted water) in the one-dimensional sand column (200mL); put 2g sodium persulfate slow-release agent at the water inlet of the one-dimensional sand column; connect the one-dimensional sand column, water tank and peristalsis Pump; start the peristaltic pump; pump water at a flow rate of 2.0 mL/min; take regular samples after starting the peristaltic pump, and measure the sodium persulfate concentration (or tetracycline concentration) of each water sample; draw the sodium persulfate concentration (or tetracycline concentration) curve.
动态释放实验:让填充好介质后的实验柱内水饱和,在一维砂柱进水口处加入2g缓释剂或者相当于2g缓释剂里过硫酸钠质量的过硫酸钠粉末。让体系内水为过硫酸钠溶液,测定其浓度随时间变化。动态释放实验中的过硫酸钠浓度随时间变化如图4所示。Dynamic release experiment: Saturate the water in the experimental column after filling the medium, and add 2g of slow-release agent or sodium persulfate powder equivalent to the quality of sodium persulfate in the 2g slow-release agent at the water inlet of the one-dimensional sand column. Let the water in the system be a sodium persulfate solution, and measure the change of its concentration with time. The variation of sodium persulfate concentration with time in the dynamic release experiment is shown in Figure 4.
动态修复实验:让实验柱介质内充满四环素污染水,初始浓度为10mg/L。在实验柱入水口处添加2g缓释剂或者相当于2g缓释剂里过硫酸钠质量的过硫酸钠粉末。连接蠕动泵和实验柱,开启蠕动泵进行动态修复实验。动态修复实验中的四环素浓度随时间变化如图5所示。Dynamic remediation experiment: Fill the experimental column medium with tetracycline-contaminated water with an initial concentration of 10 mg/
实施例4Example 4
缓释剂制备方法和实施例3的区别仅在于有序介孔氧化锰的加入量为0.3g,其余步骤和条件均相同。The difference between the preparation method of the sustained-release agent and Example 3 is only that the amount of ordered mesoporous manganese oxide added is 0.3 g, and the remaining steps and conditions are the same.
实施例5Example 5
缓释剂制备方法和实施例3的区别仅在于有序介孔氧化锰的加入量为0.7g,其余步骤和条件均相同。The difference between the preparation method of the sustained-release agent and Example 3 is only that the amount of ordered mesoporous manganese oxide added is 0.7 g, and the remaining steps and conditions are the same.
实施例6Example 6
缓释剂制备方法和实施例3的区别仅在于不加入有序介孔氧化锰且石蜡用量为3g,其余步骤和条件均相同。The only difference between the preparation method of the sustained-release agent and Example 3 is that no ordered mesoporous manganese oxide is added and the amount of paraffin wax is 3 g, and the remaining steps and conditions are the same.
实施例7Example 7
缓释剂制备方法和实施例6的区别仅在于石蜡用量为6g,其余步骤和条件均相同。The difference between the preparation method of the sustained-release agent and Example 6 is only that the amount of paraffin wax is 6 g, and the remaining steps and conditions are the same.
实施例8Example 8
缓释剂制备方法和实施例6的区别仅在于石蜡用量为12g,其余步骤和条件均相同。The difference between the preparation method of the sustained-release agent and Example 6 is only that the amount of paraffin wax is 12 g, and the remaining steps and conditions are the same.
实施例9Example 9
缓释剂制备方法和实施例8的区别仅在于过硫酸钠用量为2g,其余步骤和条件均相同。The difference between the preparation method of the sustained-release agent and Example 8 is only that the amount of sodium persulfate is 2 g, and the remaining steps and conditions are the same.
实施例10Example 10
缓释剂制备方法和实施例9的区别仅在于过硫酸钠用量为6g,其余步骤和条件均相同。The difference between the preparation method of the slow-release agent and Example 9 is only that the amount of sodium persulfate is 6 g, and the remaining steps and conditions are the same.
测试例1Test Example 1
实施例1、2的不同催化剂对四环素降解的影响变化图如图6所示。可见,不同催化材料对过硫酸钠的催化活性不同,本发明的有序介孔氧化锰具有明显更好的催化活性。商用二氧化锰不具备有序介孔结构,比表面积较小,催化性能弱,而本发明的有序介孔氧化锰表现出了良好的性能,能在吸附大量四环素的同时,又让过硫酸钠与四环素充分接触反应;并且在有序介孔氧化锰材料中观察到存在大量的Mn3+/Mn4+对,所以使其拥有良好的催化性能,因此选择有序介孔氧化锰作为缓释剂中的催化材料。Figure 6 shows the effect of different catalysts in Examples 1 and 2 on the degradation of tetracycline. It can be seen that different catalytic materials have different catalytic activities on sodium persulfate, and the ordered mesoporous manganese oxide of the present invention has significantly better catalytic activities. Commercial manganese dioxide has no ordered mesoporous structure, small specific surface area and weak catalytic performance, while the ordered mesoporous manganese oxide of the present invention shows good performance, and can adsorb a large amount of tetracycline while allowing persulfuric acid to be absorbed. Sodium and tetracycline are fully contacted and reacted; and a large number of Mn 3+ /Mn 4+ pairs are observed in the ordered mesoporous manganese oxide material, so it has good catalytic performance, so ordered mesoporous manganese oxide is selected as the catalyst. Catalytic material in release agent.
测试例2Test case 2
为了研究有序介孔氧化锰的添加量对缓释剂效果的影响,选取实施例3~5和实施例8一共4种缓释剂进行静态修复实验。不同有序介孔氧化锰比例缓释剂静态修复六小时四环素变化图如图7所示。可见,不加有序介孔氧化锰的空白对照组,对四环素几乎无降解作用,可见单纯添加过硫酸钠由于其过于稳定而对四环素几乎无氧化降解作用,要通过添加有序介孔氧化锰来活化过硫酸钠,使之生成SO4 -·来氧化四环素。而且只要添加微量的有序介孔氧化锰,就能有效催化过硫酸钠,降解四环素,且有序介孔氧化锰用量越多,缓释剂对四环素的降解作用越强,但随着添加量进一步提高,经济效益会有所降低,出于经济性考虑,催化剂添加量应与氧化剂的量相符合。所以需要控制介孔二氧化锰的添加比例以获得最佳效果。In order to study the influence of the addition amount of ordered mesoporous manganese oxide on the effect of the slow-release agent, a total of 4 kinds of slow-release agents in Examples 3 to 5 and Example 8 were selected for static repair experiments. Figure 7 shows the changes of tetracycline after static repair of slow-release agents with different proportions of ordered mesoporous manganese oxide for six hours. It can be seen that the blank control group without ordered mesoporous manganese oxide has almost no degradation effect on tetracycline. It can be seen that the simple addition of sodium persulfate has almost no oxidative degradation effect on tetracycline due to its too stability. To activate sodium persulfate to generate SO 4 - · to oxidize tetracycline. Moreover, as long as a trace amount of ordered mesoporous manganese oxide is added, it can effectively catalyze sodium persulfate and degrade tetracycline. Further increase, the economic benefits will be reduced, for economic considerations, the amount of catalyst added should be consistent with the amount of oxidant. Therefore, it is necessary to control the addition ratio of mesoporous manganese dioxide to obtain the best effect.
测试例3Test case 3
为了研究不同蜡砂比对缓释剂效果的影响,选取实施例6、7、8这3种缓释剂进行动态修复实验。不同蜡砂比的缓释剂静态释放六小时过硫酸钠变化图如图8所示。可见,蜡砂比对缓释剂的释放性能有较大影响,缓释剂中石蜡含量越多,则缓释剂的释放速率越慢。这是因为石蜡含量越多,缓释剂更加致密紧实,过硫酸钠的释放更加缓慢,石蜡含量越少,缓释剂整体就较为松散,包裹不牢固,过硫酸钠就容易从中释出。当蜡砂比为1:1时,缓释剂表现出良好的缓释性能。In order to study the effect of different wax-sand ratios on the effect of slow-release agents, three kinds of slow-release agents in Examples 6, 7, and 8 were selected to carry out dynamic repair experiments. Figure 8 shows the changes of sodium persulfate in the static release of slow-release agents with different wax-sand ratios for six hours. It can be seen that the wax-sand ratio has a great influence on the release performance of the slow-release agent. The more paraffin content in the slow-release agent, the slower the release rate of the slow-release agent. This is because the higher the paraffin content, the more compact the sustained-release agent is, and the slower the release of sodium persulfate is. When the wax-sand ratio was 1:1, the sustained-release agent showed good sustained-release performance.
测试例4Test Example 4
为了研究不同氧化剂含量对缓释剂效果的影响,选取实施例8、9、10这3种缓释剂进行动态修复实验,不同氧化剂含量缓释剂静态释放六小时过硫酸钠变化图如图9所示。可见,过硫酸钠的添加量越多,释放时过硫酸钠释出就越快。当添加量为2g时,过硫酸钠几乎没有释放,可能是由于石蜡包裹严实,导致释放效率极低;添加过硫酸钠质量为4g与6g的缓释剂释放效果相差不大。第1小时内,可以看出缓释剂的释放速率由快变慢,然后慢慢达到平衡,在接下来的5小时内,释放速率较为平稳,显示出缓释剂优异的缓释特性。可见缓释剂中氧化剂负载量越大,缓释剂释放速率会稍许加快,说明可以通过改变缓释剂中过硫酸钠的含量来调整其释放浓度,根据不同场地的污染物浓度作出相应的调整,达到最佳的治理效果。In order to study the effect of different oxidant contents on the effect of sustained-release agents, three kinds of sustained-release agents in Examples 8, 9, and 10 were selected to carry out dynamic repair experiments. shown. It can be seen that the more sodium persulfate is added, the faster the sodium persulfate is released during release. When the amount of sodium persulfate added was 2g, there was almost no release of sodium persulfate, which may be due to the tight paraffin coating, resulting in extremely low release efficiency. In the first hour, it can be seen that the release rate of the sustained-release agent changes from fast to slow, and then slowly reaches equilibrium. In the next 5 hours, the release rate is relatively stable, showing the excellent sustained-release characteristics of the sustained-release agent. It can be seen that the larger the oxidant load in the slow-release agent, the faster the release rate of the slow-release agent, which shows that the release concentration can be adjusted by changing the content of sodium persulfate in the slow-release agent, and the corresponding adjustment can be made according to the pollutant concentration of different sites. , to achieve the best governance effect.
此外应理解,在阅读了本发明的上述描述内容之后,本领域技术人员可以对本发明作各种改动或修改,这些等价形式同样落于本申请所附权利要求书所限定的范围。In addition, it should be understood that after reading the above description of the present invention, those skilled in the art can make various changes or modifications to the present invention, and these equivalent forms also fall within the scope defined by the appended claims of the present application.
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Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
AU3785599A (en) * | 1998-05-05 | 1999-11-23 | United Technologies Corporation | Chemical oxidation of volatile organic compounds |
CN102786094A (en) * | 2012-08-10 | 2012-11-21 | 同济大学 | Preparation method and application of mesoporous manganese oxide material |
CN104724815A (en) * | 2015-04-02 | 2015-06-24 | 中国科学院城市环境研究所 | The method and application of efficient and rapid removal of antipyrin by using MnOx/SBA-15-PMS composite system |
CN110280300A (en) * | 2019-06-13 | 2019-09-27 | 中国科学技术大学 | A kind of preparation method and application loading Mn oxide ordered mesoporous carbon composite material |
CN110387242A (en) * | 2019-06-27 | 2019-10-29 | 浙江工商大学 | A kind of potassium permanganate sustained-release agent and its preparation method and application |
CN111151289A (en) * | 2019-12-25 | 2020-05-15 | 浙江工商大学 | Manganese-based bimetallic oxide mesoporous materials and their preparation and application |
CN111547832A (en) * | 2020-04-16 | 2020-08-18 | 中国环境科学研究院 | A kind of persulfate gel sustained-release agent and preparation method and application |
CN111892155A (en) * | 2020-08-20 | 2020-11-06 | 江苏苏美达成套设备工程有限公司 | Slow-release oxidizing agent for removing underground water polluted organic matter and process thereof |
-
2021
- 2021-03-10 CN CN202110259970.3A patent/CN113044949B/en active Active
Patent Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
AU3785599A (en) * | 1998-05-05 | 1999-11-23 | United Technologies Corporation | Chemical oxidation of volatile organic compounds |
CN102786094A (en) * | 2012-08-10 | 2012-11-21 | 同济大学 | Preparation method and application of mesoporous manganese oxide material |
CN104724815A (en) * | 2015-04-02 | 2015-06-24 | 中国科学院城市环境研究所 | The method and application of efficient and rapid removal of antipyrin by using MnOx/SBA-15-PMS composite system |
CN110280300A (en) * | 2019-06-13 | 2019-09-27 | 中国科学技术大学 | A kind of preparation method and application loading Mn oxide ordered mesoporous carbon composite material |
CN110387242A (en) * | 2019-06-27 | 2019-10-29 | 浙江工商大学 | A kind of potassium permanganate sustained-release agent and its preparation method and application |
CN111151289A (en) * | 2019-12-25 | 2020-05-15 | 浙江工商大学 | Manganese-based bimetallic oxide mesoporous materials and their preparation and application |
CN111547832A (en) * | 2020-04-16 | 2020-08-18 | 中国环境科学研究院 | A kind of persulfate gel sustained-release agent and preparation method and application |
CN111892155A (en) * | 2020-08-20 | 2020-11-06 | 江苏苏美达成套设备工程有限公司 | Slow-release oxidizing agent for removing underground water polluted organic matter and process thereof |
Non-Patent Citations (1)
Title |
---|
锰砂活化过硫酸钠降解苯酚研究;王美茹等;《环境工程》;20171130;第35卷(第11期);第62-65页 * |
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