CN116903252A - Green and environment-friendly preparation method of porous material, product obtained by method and application of product - Google Patents
Green and environment-friendly preparation method of porous material, product obtained by method and application of product Download PDFInfo
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Abstract
本发明公开了一种多孔材料的绿色环保制备方法及所得产品和应用,该方法将固体粉末及液体磷酸溶液配料后,经由高温熔融‑水淬‑热处理,形成磷酸盐微晶玻璃颗粒,再进一步在磷酸溶液中处理得到多孔材料。在本发明中,采用磷酸来处理磷酸盐微晶玻璃,通过选择性酸蚀而形成多孔材料。酸处理后的磷酸废液可以作为玻璃原料循环利用,大大降低了生产成本,避免了环境污染,为多孔材料的大规模工业化生产创造了条件,是一种绿色环保的合成方法。此外,合成的多孔材料具有两种光催化功能晶相,且不含显著的易分解的带结晶水晶相,热稳定性高,可广泛应用在吸附、催化降解有机污染物、污水处理、光热催化、高温催化等领域。
The invention discloses a green and environmentally friendly preparation method of porous materials and the resulting products and applications. In this method, solid powder and liquid phosphoric acid solution are batched, and then undergo high-temperature melting-water quenching-heat treatment to form phosphate glass-ceramic particles, and then further Treatment in phosphoric acid solution yields porous materials. In the present invention, phosphoric acid is used to treat phosphate glass-ceramics, and porous materials are formed by selective acid etching. The phosphoric acid waste liquid after acid treatment can be recycled as glass raw material, which greatly reduces production costs, avoids environmental pollution, and creates conditions for large-scale industrial production of porous materials. It is a green and environmentally friendly synthesis method. In addition, the synthesized porous material has two photocatalytic functional crystal phases and does not contain an obvious crystalline phase that is easily decomposed. It has high thermal stability and can be widely used in adsorption, catalytic degradation of organic pollutants, sewage treatment, photothermal Catalysis, high temperature catalysis and other fields.
Description
技术领域Technical field
本发明涉及一种多孔材料的绿色环保制备方法及所得产品,还涉及该多孔材料在吸附和光催化领域的应用,属于多孔材料制备技术领域。The invention relates to a green and environmentally friendly preparation method of porous materials and the resulting products. It also relates to the application of the porous materials in the fields of adsorption and photocatalysis, and belongs to the technical field of porous material preparation.
背景技术Background technique
多孔材料由于具有较大的比表面积、吸附容量和许多特殊的性能,在吸附、分离、CO2还原、光热催化、中高温脱硫脱硝催化剂载体等领域得到广泛的应用。多孔材料的合成方法很多,有溶胶-凝胶法、水热合成法、沉淀法和化学腐蚀法等合成方法。其中,溶胶-凝胶法、水热合成法、沉淀法均是基于化学反应在溶液中进行,统称为湿化学法,是一种自下而上的合成路径,其产能较低,生产成本较高,大规模工业生产困难。化学腐蚀法则是一种自上而下的模式,通常先获得某种块体无孔材料,再经过酸化学腐蚀选择性溶出部分物质,从而形成多孔骨架材料。这一方法的优势可采用工业化大规模生产途径先大量制备块体无孔材料,再通过酸蚀得到多孔材料,但该方法的缺点是在酸蚀过程中会溶出部分物质,造成材料的浪费,同时酸腐蚀会产生大量酸性废液,后续的回收处理会产生高额的费用,增加生产成本,造成环境污染。Due to their large specific surface area, adsorption capacity and many special properties, porous materials are widely used in the fields of adsorption, separation, CO2 reduction, photothermal catalysis, medium and high temperature desulfurization and denitrification catalyst carriers and other fields. There are many synthesis methods for porous materials, including sol-gel method, hydrothermal synthesis method, precipitation method and chemical etching method. Among them, the sol-gel method, hydrothermal synthesis method, and precipitation method are all based on chemical reactions in solution. They are collectively called wet chemical methods. They are a bottom-up synthesis path with low productivity and relatively high production costs. High, large-scale industrial production is difficult. The chemical corrosion law is a top-down model. Usually, a certain bulk non-porous material is first obtained, and then some substances are selectively dissolved through acid chemical corrosion to form a porous skeleton material. The advantage of this method is that industrial large-scale production can be used to prepare bulk non-porous materials in large quantities first, and then the porous materials can be obtained through acid etching. However, the disadvantage of this method is that some substances will be dissolved during the acid etching process, resulting in a waste of materials. At the same time, acid corrosion will produce a large amount of acidic waste liquid, and subsequent recycling and treatment will incur high costs, increase production costs, and cause environmental pollution.
在多孔玻璃或多孔微晶玻璃生产技术中,常用的腐蚀介质为酸性溶液(如:盐酸、硫酸等),因为玻璃本身耐酸不耐碱,利用酸做为腐蚀液可留下玻璃骨架而选择性蚀除玻璃中部分组分和结构,从而形成多孔结构和材料。然而盐酸、硫酸溶液具有强腐蚀性和挥发性,会损害生产人员的身体健康,同时酸液本身及生产过程中产生的废液还会对环境造成严重的污染和危害。因此,酸蚀法制备多孔材料的环境安全性及酸性废液的回收处理成为化学腐蚀法制备多孔材料的制约性难题,寻找安全可代替的酸蚀方法成为迫切需求。In the production technology of porous glass or porous glass-ceramics, the commonly used corrosive medium is acidic solution (such as hydrochloric acid, sulfuric acid, etc.). Since the glass itself is acid-resistant and not alkali-resistant, using acid as the corrosive liquid can leave the glass skeleton and be selective. Etching away some components and structures in the glass to form porous structures and materials. However, hydrochloric acid and sulfuric acid solutions are highly corrosive and volatile, which will damage the health of production personnel. At the same time, the acid itself and the waste liquid generated during the production process will also cause serious pollution and harm to the environment. Therefore, the environmental safety of porous materials prepared by acid etching and the recycling of acidic waste liquid have become restrictive problems in the preparation of porous materials by chemical etching. Finding safe and alternative acid etching methods has become an urgent need.
此外,多孔材料为多孔骨架结构,高温稳定性较差,在高温使用过程中存在坍塌的可能,特别是当多孔骨架本身组成中含带结晶水或易分解的物质时,此现象表现更加突出。多孔结构一旦坍塌,孔道即部分或全部消失,阻碍物质的进出,表面积急剧减小,因而其在吸附、分离、催化等领域的应用受限,严重时将无法使用,彻底丧失多孔材料的功能和优势。在TiO2含量高的铜钛磷酸盐微晶玻璃体系中,此问题尤其突出。此前的研究表明(A glass-ceramic approach to prepare porous TiO2with self-supported nano-flakes: Thephase evolution and the thermal stability of the product),使用盐酸处理后获得的多孔材料,因含有Ti(HPO4)2⋅2H2O晶相,当其经过高温煅烧后构成材料多孔结构的纳米片全部坍塌,孔道全部消失,多孔结构不复存在,丧失其可在高温条件下使用的优势。In addition, porous materials have a porous skeleton structure, which has poor high-temperature stability and may collapse during high-temperature use. This phenomenon becomes more prominent, especially when the porous skeleton itself contains crystal water or easily decomposable substances. Once the porous structure collapses, the pores will disappear partially or completely, hindering the entry and exit of substances, and the surface area will decrease sharply. Therefore, its application in the fields of adsorption, separation, catalysis, etc. is limited. In severe cases, it will be unusable and the functions and functions of the porous material will be completely lost. Advantage. This problem is particularly prominent in copper-titanium phosphate glass-ceramic systems with high TiO content. Previous research has shown that (A glass-ceramic approach to prepare porous TiO 2 with self-supported nano-flakes: Thephase evolution and the thermal stability of the product), the porous material obtained after treatment with hydrochloric acid contains Ti(HPO 4 ) 2⋅2H 2 O crystal phase, when it is calcined at high temperature, all the nanosheets that constitute the porous structure of the material collapse, all the pores disappear, the porous structure no longer exists, and the advantage of being used under high temperature conditions is lost.
发明内容Contents of the invention
针对现有上述多孔材料在制备及高温稳定性上存在的不足,本发明提供了一种多孔材料的绿色环保制备方法,该制备方法利用磷酸溶液作为磷酸盐微晶玻璃的原料,同时采用磷酸作为酸处理的酸性溶液,避免了强腐蚀性和挥发性的HCl、H2SO4溶液的使用,提高了使用安全性,并且酸处理采用与玻璃合成原料同源、与待酸蚀基质体系特征相同的磷酸作为腐蚀液,酸处理后产生的废液可以作为原料回用,为废液的再利用创造了条件,实现了多孔材料的绿色环保制备。同时,本发明经过磷酸处理得到的多孔材料高温稳定性强,经750℃的高温煅烧后仍保持着原有的多孔结构,没有出现孔道坍塌、消失情况,更适合在高温条件下使用。In view of the shortcomings in the preparation and high-temperature stability of the existing porous materials, the present invention provides a green and environmentally friendly preparation method of porous materials. The preparation method uses phosphoric acid solution as the raw material of phosphate glass-ceramics, and uses phosphoric acid as the raw material. The acidic solution for acid treatment avoids the use of highly corrosive and volatile HCl and H 2 SO 4 solutions, improving the safety of use. The acid treatment uses the same source as the glass synthetic raw material and has the same characteristics as the matrix system to be acid-etched. Phosphoric acid is used as a corrosive liquid, and the waste liquid generated after acid treatment can be reused as raw material, creating conditions for the reuse of waste liquid and realizing the green and environmentally friendly preparation of porous materials. At the same time, the porous material obtained by the phosphoric acid treatment of the present invention has strong high-temperature stability. After being calcined at a high temperature of 750°C, it still maintains the original porous structure without pore collapse or disappearance, and is more suitable for use under high temperature conditions.
本发明具体技术方案如下:The specific technical solutions of the present invention are as follows:
一种多孔材料的绿色环保制备方法,该方法包括以下步骤:A green and environmentally friendly preparation method of porous materials, which method includes the following steps:
(1)根据MgO-CuO-TiO2-P2O5的玻璃配方组成,称取各原料,将各原料混合均匀,得到玻璃配合料;(1) According to the glass formula composition of MgO-CuO-TiO 2 -P 2 O 5 , weigh each raw material and mix each raw material evenly to obtain a glass batch;
(2)将玻璃配合料高温熔融,得到玻璃熔体,将玻璃熔体水淬、干燥,得到母体玻璃;(2) Melt the glass batch material at high temperature to obtain a glass melt, then quench and dry the glass melt to obtain the parent glass;
(3)将母体玻璃依次升至其玻璃转变温度和第一玻璃析晶峰温度附近进行热处理,得到热处理玻璃;(3) The parent glass is sequentially raised to its glass transition temperature and near the first glass crystallization peak temperature for heat treatment to obtain heat-treated glass;
(4)将热处理玻璃放入磷酸溶液中进行酸处理,酸处理后水洗、干燥,得到多孔材料。(4) Put the heat-treated glass into a phosphoric acid solution for acid treatment. After acid treatment, wash with water and dry to obtain a porous material.
进一步的,步骤(1)中,MgO由氧化镁引入,CuO由氧化铜引入,TiO2由二氧化钛引入,P2O5由磷酸溶液引入。磷酸溶液的浓度没有特别要求,只要能够引入所需量的P2O5即可。Further, in step (1), MgO is introduced from magnesium oxide, CuO is introduced from copper oxide, TiO 2 is introduced from titanium dioxide, and P 2 O 5 is introduced from phosphoric acid solution. There is no special requirement for the concentration of the phosphoric acid solution, as long as the required amount of P 2 O 5 can be introduced.
进一步的,步骤(1)中,玻璃配方中,MgO所占的摩尔含量为15~25%,CuO所占的摩尔含量为20~30%,TiO2所占的摩尔含量为30~38%,P2O5所占的摩尔含量为20~30%,这四者摩尔含量之和为100%。优选的,MgO所占的摩尔含量为20%,CuO所占的摩尔含量为24%,TiO2所占的摩尔含量为32%,P2O5所占的摩尔含量为24%。Further, in step (1), in the glass formula, the molar content of MgO is 15~25%, the molar content of CuO is 20~30%, and the molar content of TiO2 is 30~38%. The molar content of P 2 O 5 is 20~30%, and the sum of the molar contents of these four is 100%. Preferably, the molar content of MgO is 20%, the molar content of CuO is 24%, the molar content of TiO 2 is 32%, and the molar content of P 2 O 5 is 24%.
进一步的,步骤(1)中,原料的混合顺序为:首先将氧化镁、氧化铜、二氧化钛粉料混合均匀,再缓慢加入磷酸溶液混合成浆状,如果混合料无法成浆状,则再加入水使混合料成浆状;混合均匀后将混合料在150~250℃下处理至水分蒸干,然后粉碎并充分混合,得到玻璃配合料。在进行加热处理20~30小时,然后粉碎并充分混合,得到玻璃配合料。混合料在150~250℃下加热处理的目的是为了将配合料中的水分蒸发形成结块泥料,然后将这种结块的泥料进行研磨,得到混合均匀的粉末配合料。同时将各原料混合均匀后再进行加热处理,只会使得水分蒸发,保证玻璃组成不变。加热温度为可以为150℃、160℃、170℃、180℃、190℃、200℃、21℃、220℃、230℃、240℃、250℃,优选为200℃。加热处理至混合料成结块的泥料即可,根据水量的不同时间不同。在本发明某一具体实施方式中,处理时间一般为20~30小时,例如20小时、21小时、22小时、23小时、24小时、25小时、26小时、27小时、28小时、29小时、30小时。Further, in step (1), the mixing sequence of the raw materials is: first mix the magnesium oxide, copper oxide, and titanium dioxide powder evenly, then slowly add the phosphoric acid solution and mix it into a slurry. If the mixture cannot become a slurry, then add Water makes the mixture into a slurry; after mixing evenly, the mixture is treated at 150~250°C until the water evaporates to dryness, then crushed and thoroughly mixed to obtain a glass batch. Heat treatment for 20 to 30 hours, then crush and mix thoroughly to obtain glass batch. The purpose of heating the mixture at 150~250℃ is to evaporate the water in the batch to form agglomerated mud, and then grind the agglomerated mud to obtain a uniformly mixed powder batch. At the same time, mixing the raw materials evenly before heating will only evaporate the water and ensure that the composition of the glass remains unchanged. The heating temperature can be 150°C, 160°C, 170°C, 180°C, 190°C, 200°C, 21°C, 220°C, 230°C, 240°C, or 250°C, and is preferably 200°C. Heat treatment until the mixture becomes agglomerated mud. The time will vary depending on the amount of water. In a specific embodiment of the present invention, the processing time is generally 20 to 30 hours, such as 20 hours, 21 hours, 22 hours, 23 hours, 24 hours, 25 hours, 26 hours, 27 hours, 28 hours, 29 hours, 30 hours.
进一步的,步骤(2)中,玻璃配合料高温熔融的步骤为:将玻璃配合料以3~8℃/min的升温速率从室温升到1200~1500℃,然后在1200~1500℃保温1~2小时,使得配合料完全熔融,得到玻璃熔体。优选的,将玻璃配合料以5℃/min的升温速率升温至1350℃,并保温1小时。Further, in step (2), the step of high-temperature melting of the glass batch material is: raising the glass batch material from room temperature to 1200~1500°C at a heating rate of 3~8°C/min, and then maintaining the temperature at 1200~1500°C for 1 ~2 hours, the batch materials are completely melted, and the glass melt is obtained. Preferably, the glass batch is heated to 1350°C at a heating rate of 5°C/min and kept warm for 1 hour.
进一步的,步骤(2)中,水淬是指将所得玻璃熔体倒入水中,形成玻璃状态。收集水淬后的玻璃料,干燥,即为母体玻璃。Further, in step (2), water quenching means pouring the obtained glass melt into water to form a glass state. Collect the water-quenched glass frit and dry it to become the parent glass.
进一步的,步骤(3)中,水淬干燥后的母体玻璃进行DTA测试,可以得到DTA曲线。从DTA曲线中可以得到玻璃转变温度和玻璃第一析晶峰温度(玻璃转变温度及玻璃第一析晶峰温度是DTA曲线中的两个峰值)。将母体玻璃先升温至玻璃转变温度热处理1~2小时,然后再升温至玻璃第一析晶峰温度附近热处理2~3小时,然后随炉冷却,得到热处理玻璃,该热处理玻璃为磷酸盐微晶玻璃。如果玻璃第一析晶峰温度为T℃,则玻璃第一析晶峰温度附近的温度为T℃~(T+20)℃的温度范围。Further, in step (3), the parent glass after water quenching and drying is subjected to DTA testing, and a DTA curve can be obtained. The glass transition temperature and the first crystallization peak temperature of glass can be obtained from the DTA curve (the glass transition temperature and the first crystallization peak temperature of glass are the two peaks in the DTA curve). The parent glass is first heated to the glass transition temperature and heat treated for 1 to 2 hours, and then heated to near the first crystallization peak temperature of the glass for 2 to 3 hours, and then cooled in the furnace to obtain heat-treated glass, which is phosphate microcrystalline Glass. If the temperature of the first crystallization peak of glass is T°C, then the temperature near the first crystallization peak temperature of glass is in the temperature range of T°C to (T+20)°C.
进一步的,步骤(3)中,母体玻璃优选以4~5℃/min的升温速率升至其玻璃转变温度进行热处理,然后继续以该升温速率升至玻璃第一析晶峰温度附近进行热处理。Further, in step (3), the parent glass is preferably heated to its glass transition temperature at a heating rate of 4~5°C/min for heat treatment, and then continues to be heat treated at a heating rate near the first crystallization peak temperature of the glass.
进一步的,步骤(4)中,磷酸溶液的浓度为2~5mol/L,例如2mol/L、3mol/L、4mol/L、5mol/L,优选为3mol/L。Further, in step (4), the concentration of the phosphoric acid solution is 2~5 mol/L, such as 2 mol/L, 3 mol/L, 4 mol/L, 5 mol/L, preferably 3 mol/L.
进一步的,步骤(4)中,热处理玻璃的质量与磷酸溶液的体积比为1g:50ml~1g:200ml,例如1g:50ml、1g:60ml、1g:70ml、1g:80ml、1g:90ml、1g:100ml、1g:110ml、1g:120ml、1g:130ml、1g:140ml、1g:150ml、1g:160ml、1g:170ml、1g:180ml、1g:190ml、1g:200ml,优选为1g:100ml。Further, in step (4), the volume ratio of the mass of the heat-treated glass to the phosphoric acid solution is 1g:50ml~1g:200ml, such as 1g:50ml, 1g:60ml, 1g:70ml, 1g:80ml, 1g:90ml, 1g : 100ml, 1g: 110ml, 1g: 120ml, 1g: 130ml, 1g: 140ml, 1g: 150ml, 1g: 160ml, 1g: 170ml, 1g: 180ml, 1g: 190ml, 1g: 200ml, preferably 1g: 100ml.
进一步的,步骤(4)中,酸处理时,将热处理玻璃和磷酸溶液的混合物在密闭的容器中进行酸处理,目的是防止磷酸溶液挥发,并给酸处理提供一定的压力条件。例如可以将该混合物放入带有盖子的容器中进行酸处理,或者是将混合物装入烧杯等敞口容器中,然后将容器口采用聚乙烯薄膜等材料进行密封。优选的,将混合物在烧杯中进行酸处理,采用3~5层的聚乙烯薄膜对烧杯进行密封。Further, in step (4), during acid treatment, the mixture of heat-treated glass and phosphoric acid solution is acid-treated in a sealed container to prevent the phosphoric acid solution from volatilizing and to provide certain pressure conditions for the acid treatment. For example, the mixture can be put into a container with a lid for acid treatment, or the mixture can be put into an open container such as a beaker, and then the mouth of the container can be sealed with a material such as polyethylene film. Preferably, the mixture is acid-treated in a beaker, and the beaker is sealed with 3 to 5 layers of polyethylene film.
进一步的,步骤(4)中,酸处理的温度为50~100℃,例如50℃、60℃、70℃、80℃、90℃、100℃,优选为100℃。磷酸酸处理所需时间比盐酸、硫酸所需时间长,大多为24-96h,例如24h、30h、36h、40h、48h、55h、60h、70h、80h、90h、96h,优选为48h。Further, in step (4), the acid treatment temperature is 50 to 100°C, such as 50°C, 60°C, 70°C, 80°C, 90°C, 100°C, preferably 100°C. The time required for phosphoric acid treatment is longer than that of hydrochloric acid and sulfuric acid, mostly 24-96h, such as 24h, 30h, 36h, 40h, 48h, 55h, 60h, 70h, 80h, 90h, 96h, preferably 48h.
进一步的,步骤(4)中,酸处理完成后,分离玻璃样品和磷酸废液,将酸处理后的玻璃样品进行水洗,干燥,得到最终的多孔材料。水洗的操作为:将酸处理后的玻璃样品加入与磷酸溶液等体积的水中,浸泡玻璃样品2~3小时,然后用水冲洗玻璃样品3-5次。Further, in step (4), after the acid treatment is completed, the glass sample and the phosphoric acid waste liquid are separated, and the acid-treated glass sample is washed and dried to obtain the final porous material. The water washing operation is as follows: add the acid-treated glass sample to an equal volume of water as the phosphoric acid solution, soak the glass sample for 2 to 3 hours, and then rinse the glass sample with water 3 to 5 times.
进一步的,步骤(4)中,磷酸废液中含量大量的磷酸,还含有部分Mg2+、Cu2+和Ti4+离子,这些都是玻璃的组成元素,因此该磷酸废液可以直接作为玻璃原料回用至步骤(1)中,可以仅以磷酸废液作为P2O5的唯一原料,也可以将磷酸废液和纯度的磷酸溶液共同作为P2O5的原料。这样可以实现废酸溶液的回收利用,避免了废酸的排放,解决了废酸污染环境、后处理等问题,更加绿色环保。磷酸废液进行回用时,可以先对其中的P5+、Mg2+、Cu2+和Ti4+含量进行检测,然后将磷酸废液作为 P2O5的原料回用,同时计算废液引入的Mg、Cu、Ti的量,根据玻璃配方计算除了废液外还需要的纯磷酸溶液、氧化镁、氧化铜、二氧化钛的量,缺少的部分再由这些纯原料进行补充。磷酸废液的浓度没有特殊要求。Furthermore, in step (4), the phosphoric acid waste liquid contains a large amount of phosphoric acid and also contains some Mg 2+ , Cu 2+ and Ti 4+ ions, which are all constituent elements of glass, so the phosphoric acid waste liquid can be directly used as The glass raw material is reused in step (1), and the phosphoric acid waste liquid can be used as the only raw material of P 2 O 5 , or the phosphoric acid waste liquid and the pure phosphoric acid solution can be used as the raw materials of P 2 O 5 . This can realize the recycling of waste acid solution, avoid the discharge of waste acid, solve the problems of environmental pollution and post-processing of waste acid, and make it more green and environmentally friendly. When reusing the phosphoric acid waste liquid, you can first detect the P 5+ , Mg 2+ , Cu 2+ and Ti 4+ contents, and then reuse the phosphoric acid waste liquid as a raw material for P 2 O 5 and calculate the waste liquid at the same time The amount of Mg, Cu, and Ti introduced is calculated according to the glass formula, and the amount of pure phosphoric acid solution, magnesium oxide, copper oxide, and titanium dioxide required in addition to the waste liquid is calculated. The missing parts are then supplemented by these pure raw materials. There are no special requirements for the concentration of phosphoric acid waste liquid.
本发明制备方法采用磷酸作为玻璃原料,同时作为磷酸作为玻璃酸处理的酸溶液,酸处理后的磷酸废液可以作为玻璃原料回用,大大提高了制备的安全性和绿色环保性,还降低了制备成本。同时,经SEM分析表明,本发明磷酸处理得到的多孔材料为纳米片构成的多孔骨架(见图3)。经XRD分析表明,该多孔材料同时存在两种具有光催化功能的晶相——MgTi4(PO4)6和锐钛型TiO2相(见图2),且不含显著的导致其受热分解、孔结构塌陷的Ti(HPO4)2•2H2O晶相,在750℃煅烧后孔结构仍不塌陷(见图4),因此该多孔材料高温稳定性强耐高温性能优异,在高温环境下使用具有更好的优势。The preparation method of the present invention uses phosphoric acid as the glass raw material and at the same time as the acid solution for hyaluronic acid treatment. The phosphoric acid waste liquid after the acid treatment can be reused as the glass raw material, which greatly improves the safety and green environmental protection of the preparation, and also reduces the cost. Preparation costs. At the same time, SEM analysis shows that the porous material obtained by the phosphoric acid treatment of the present invention is a porous skeleton composed of nanosheets (see Figure 3). XRD analysis shows that this porous material simultaneously contains two crystal phases with photocatalytic functions - MgTi 4 (PO 4 ) 6 and anatase TiO 2 phases (see Figure 2), and does not contain significant thermal decomposition , Ti(HPO 4 ) 2• 2H 2 O crystal phase with collapsed pore structure, the pore structure does not collapse after calcination at 750℃ (see Figure 4), so this porous material has strong high temperature stability and excellent high temperature resistance, and can be used in high temperature environments It has better advantages when used below.
进一步的,本发明多孔材料可以作为吸附剂、光催化剂等进行使用,因此该多孔材料作为吸附剂、光催化剂的应用也在本发明保护范围之内。Furthermore, the porous material of the present invention can be used as an adsorbent, a photocatalyst, etc., so the application of the porous material as an adsorbent or a photocatalyst is also within the scope of the present invention.
进一步的,本发明的多孔材料在高温下具有较好的稳定性,至少在750℃下的高温下稳定性较好。因此,本发明还提供了该多孔材料作为光热催化剂或高温催化剂载体的应用。Furthermore, the porous material of the present invention has good stability at high temperatures, at least at a high temperature of 750°C. Therefore, the present invention also provides the application of the porous material as a photothermal catalyst or a high-temperature catalyst carrier.
与现有材料和技术相比,本发明的有益效果为:Compared with existing materials and technologies, the beneficial effects of the present invention are:
1、本发明提供的多孔材料的制备方法中,使用挥发性小、腐蚀性小、对环境毒性小、与合成用材料同源的磷酸溶液作为原料,同时采用磷酸溶液对磷酸盐微晶玻璃基体进行腐蚀,形成多孔材料,所得的磷酸废液可以作为原料回用,实现了生产废液的回收与生产再利用。1. In the preparation method of porous materials provided by the present invention, a phosphoric acid solution with low volatility, low corrosiveness, low environmental toxicity, and homologous to synthetic materials is used as a raw material, and the phosphoric acid solution is used to treat the phosphate glass-ceramic matrix. Corrosion is carried out to form porous materials, and the resulting phosphoric acid waste liquid can be reused as raw material, realizing the recovery and production reuse of production waste liquid.
2、本发明制备过程易产业化,生产过程易控制,适合于工业化制备多孔材料。另外制备过程实现了材料的循环利用,大大降低了生产成本,避免了环境污染,绿色环保,符合可持续发展的理念,对于多孔材料的大规模工业化推广和商业应用具有重要意义。2. The preparation process of the present invention is easy to be industrialized, the production process is easy to control, and is suitable for industrial preparation of porous materials. In addition, the preparation process realizes the recycling of materials, greatly reduces production costs, avoids environmental pollution, is green and environmentally friendly, and conforms to the concept of sustainable development. It is of great significance for the large-scale industrial promotion and commercial application of porous materials.
3、本发明采用磷酸溶液为酸处理侵蚀液,改变了磷酸盐微晶玻璃中各元素的浸出,也改变了原位晶相生成的动力学,其结果是显著抑制了带结晶水的Ti(HPO4)2•2H2O晶相的生成,从而提高了生成的多孔材料骨架的高温稳定性,使其在高温环境下使用更有优势。3. The present invention uses phosphoric acid solution as the acid treatment etching liquid, which changes the leaching of various elements in the phosphate glass-ceramics and also changes the kinetics of in-situ crystal phase generation. The result is that the Ti with crystal water is significantly suppressed ( The formation of HPO 4 ) 2• 2H 2 O crystal phase improves the high-temperature stability of the generated porous material skeleton, making it more advantageous for use in high-temperature environments.
4、本发明方法所得多孔材料具有两种复合光催化功能晶相以及良好的吸附降解性能,可广泛应用在吸附、催化降解有机污染物、污水处理、光热催化、高温催化等领域。4. The porous material obtained by the method of the present invention has two composite photocatalytic functional crystal phases and good adsorption and degradation performance, and can be widely used in adsorption, catalytic degradation of organic pollutants, sewage treatment, photothermal catalysis, high temperature catalysis and other fields.
附图说明Description of the drawings
图1为母体玻璃的DTA曲线。Figure 1 shows the DTA curve of the parent glass.
图2为多孔材料的XRD图谱。Figure 2 shows the XRD pattern of porous materials.
图3为多孔材料的扫描电镜图片。Figure 3 is a scanning electron microscope picture of porous materials.
图4为多孔材料高温煅烧后的扫描电镜图片。Figure 4 is a scanning electron microscope picture of porous materials after high-temperature calcination.
图5为多孔材料的N2等温吸附曲线。Figure 5 shows the N2 isotherm adsorption curve of porous materials.
图6为回收的酸处理后的磷酸溶液中Mg、Cu、Ti 和 P离子的浓度。Figure 6 shows the concentrations of Mg, Cu, Ti and P ions in the recovered phosphoric acid solution after acid treatment.
具体实施方式Detailed ways
为使本发明要解决的材料和技术问题、技术方案和优点更加清楚,下面将结合附图和具体实施例进行详细描述。In order to make the material and technical problems, technical solutions and advantages to be solved by the present invention clearer, a detailed description will be given below with reference to the accompanying drawings and specific embodiments.
如果实施例中未注明的实验具体条件,通常按照常规条件,或者按照试剂公司所推荐的条件;下述实施例中所用的试剂、耗材等,如无特殊说明,均可通过商业途径获得。If the specific experimental conditions are not specified in the examples, conventional conditions are usually followed, or conditions recommended by the reagent company; the reagents, consumables, etc. used in the following examples can all be obtained through commercial channels unless otherwise specified.
本发明实验结果通过以下方法获得:采用综合热分析仪对玻璃进行差热分析(DTA)。采用X-射线衍射仪,获得样品的衍射图谱,并进行物相分析。采用扫描电子显微镜获得样品的表面微观形貌。采用氮气等温吸附仪测定样品N2等温吸附曲线,根据BET模型计算比表面积,根据BJH模型得孔径分布曲线,并由曲线峰值点数据确定孔径,孔容由N2吸附曲线相对压力最大处的吸附量确定。The experimental results of the present invention are obtained by the following method: using a comprehensive thermal analyzer to perform differential thermal analysis (DTA) on the glass. Use an X-ray diffractometer to obtain the diffraction pattern of the sample and conduct phase analysis. Scanning electron microscopy was used to obtain the surface micromorphology of the sample. Use a nitrogen isothermal adsorption instrument to measure the N 2 isothermal adsorption curve of the sample, calculate the specific surface area according to the BET model, obtain the pore size distribution curve according to the BJH model, and determine the pore size from the peak point data of the curve. The pore volume is determined by the adsorption at the maximum relative pressure of the N 2 adsorption curve. Quantity determined.
实施例1Example 1
一种多孔材料的制备方法,包括以下步骤:A method for preparing porous materials, including the following steps:
1.母体玻璃的制备1. Preparation of parent glass
根据MgO-CuO-TiO2-P2O5的玻璃配方组成,选择轻质氧化镁、氧化铜、二氧化钛、85wt%的磷酸溶液为原料,按照MgO:CuO:TiO2:P2O5= 20:24:32:24的摩尔比准确称取各原料,先将氧化镁、氧化铜和二氧化钛进行初步的混合,然后缓慢加入85wt%的磷酸溶液,并加入适量的蒸馏水混合均匀,使其呈现泥浆状态;混合均匀后将混合物在200℃下加热处理24小时,混合物水分蒸干成结块的泥料,然后将泥料粉碎并充分混合,得到玻璃配合料。将玻璃配合料装入氧化铝坩埚中,并在诺巴迪高温升降炉中对玻璃配合料进行高温熔融,熔融过程是:以5℃/min的升温速率,将温度从室温升到1350℃,然后在1350℃保温1小时,以此使得配合料完全熔融,得到玻璃熔体。高温熔融结束后,将玻璃熔体快速倒入水中,进行水淬。收集水淬后的玻璃料、干燥,此样品即为母体玻璃。According to the glass formula composition of MgO-CuO-TiO 2 -P 2 O 5 , light magnesium oxide, copper oxide, titanium dioxide, and 85wt% phosphoric acid solution are selected as raw materials. According to MgO: CuO: TiO 2 : P 2 O 5 = 20 : 24:32:24 molar ratio. Accurately weigh each raw material. First, preliminarily mix magnesium oxide, copper oxide and titanium dioxide, then slowly add 85wt% phosphoric acid solution, and add an appropriate amount of distilled water to mix evenly to make it appear as a mud. State; after mixing evenly, the mixture is heated at 200°C for 24 hours. The water in the mixture is evaporated into agglomerated mud, and then the mud is crushed and fully mixed to obtain a glass batch. Put the glass batch material into an alumina crucible, and perform high-temperature melting of the glass batch material in the Nobadi high-temperature lifting furnace. The melting process is: raising the temperature from room temperature to 1350°C at a heating rate of 5°C/min. , and then kept at 1350°C for 1 hour to completely melt the batch materials and obtain a glass melt. After the high-temperature melting is completed, the glass melt is quickly poured into water for water quenching. Collect the water-quenched glass frit and dry it. This sample is the parent glass.
2.热处理玻璃的制备2. Preparation of heat-treated glass
使用HCT-4型综合热分析仪对母体玻璃进行DTA测试,得到母体玻璃的DTA曲线(见图1)。然后将一定量的步骤1中的母体玻璃以5℃/min的升温速率升至其玻璃转变温度(622℃)热处理1小时,然后继续以5℃/min的升温速率升温至玻璃第一析晶峰温度(716℃)热处理2小时,然后随炉冷却,得到热处理玻璃。Use the HCT-4 comprehensive thermal analyzer to conduct DTA testing on the parent glass, and obtain the DTA curve of the parent glass (see Figure 1). Then heat a certain amount of the parent glass in step 1 to its glass transition temperature (622°C) at a heating rate of 5°C/min for 1 hour, and then continue to heat it at a heating rate of 5°C/min until the first crystallization of the glass. Heat treatment at the peak temperature (716°C) for 2 hours, and then cool with the furnace to obtain heat-treated glass.
3.多孔材料的制备3. Preparation of porous materials
将一定量的步骤2中的热处理玻璃和3mol/L的磷酸溶液按照1g:100ml的比例加入烧杯中,使用三层聚乙烯薄膜将烧杯口密封,然后将烧杯放入100℃的烘干箱中酸处理48h。酸处理结束后,将磷酸溶液倒出并将其回收,然后使用与磷酸溶液等体积的蒸馏水浸泡玻璃样品2小时,然后使用蒸馏水冲洗玻璃样品3次,烘干后得到多孔材料样品。Add a certain amount of the heat-treated glass in step 2 and 3mol/L phosphoric acid solution into the beaker at the ratio of 1g:100ml, seal the mouth of the beaker with three layers of polyethylene film, and then put the beaker into a drying oven at 100°C Acid treatment for 48h. After the acid treatment, pour out the phosphoric acid solution and recover it, then soak the glass sample with an equal volume of distilled water as the phosphoric acid solution for 2 hours, then rinse the glass sample with distilled water three times, and dry it to obtain a porous material sample.
对所得多孔材料进行XRD分析,结果显示多孔材料晶相以MgTi4(PO4)6为主晶相,还含有锐钛型TiO2晶相(见图2)。样品的SEM图像如图3所示,可以看出样品表面生长着大量纳米片,同时纳米片相互之间连接构成了多孔结构。该样品的N2吸附等温曲线呈现出明显的Ⅳ型吸附等温线,具有H3型回滞环,表明样品是介孔结构,孔径多分布在2-20nm之间(见图5),样品表面积和孔容分别达到了16.77m2/g,0.074cm3/g。XRD analysis of the obtained porous material showed that the crystal phase of the porous material is mainly MgTi 4 (PO 4 ) 6 and also contains anatase TiO 2 crystal phase (see Figure 2). The SEM image of the sample is shown in Figure 3. It can be seen that a large number of nanosheets grow on the surface of the sample, and the nanosheets are connected to each other to form a porous structure. The N 2 adsorption isotherm curve of this sample shows an obvious type IV adsorption isotherm with an H3 type hysteresis loop, indicating that the sample has a mesoporous structure and the pore diameter is mostly distributed between 2-20nm (see Figure 5). The surface area of the sample and The pore volumes reached 16.77m 2 /g and 0.074cm 3 /g respectively.
实施例2Example 2
一种多孔材料的制备方法,包括以下步骤:A method for preparing porous materials, including the following steps:
1.母体玻璃的制备1. Preparation of parent glass
使用电感耦合等离子体光谱仪(Agilent ICPOES730)对实施例1回收的酸处理后的磷酸溶液中的Mg、Cu、Ti 和 P离子的浓度进行测量(见图6)。使用该回收的酸处理后的磷酸溶液作为P2O5的原料,P2O5完全由该回收的磷酸溶液引入。根据MgO-CuO-TiO2-P2O5的玻璃配方组成,按照MgO:CuO:TiO2:P2O5= 20:24:32:24的摩尔比计算所需P2O5的用量,根据计算结果,同时计算得出酸处理磷酸溶液中一同引入的Mg、Cu、Ti的含量,最后计算剩余所需的MgO,CuO和TiO2的量并使用氧化镁、氧化铜和二氧化钛引入。An inductively coupled plasma spectrometer (Agilent ICPOES730) was used to measure the concentrations of Mg, Cu, Ti and P ions in the acid-treated phosphoric acid solution recovered in Example 1 (see Figure 6). The recovered acid-treated phosphoric acid solution is used as the raw material of P 2 O 5 , and P 2 O 5 is completely introduced from the recovered phosphoric acid solution. According to the glass formula composition of MgO-CuO-TiO 2 -P 2 O 5 , calculate the required amount of P 2 O 5 according to the molar ratio of MgO: CuO: TiO 2 : P 2 O 5 = 20:24:32:24, Based on the calculation results, the contents of Mg, Cu, and Ti introduced together in the acid-treated phosphoric acid solution are also calculated. Finally, the remaining required amounts of MgO, CuO, and TiO are calculated and introduced using magnesium oxide, copper oxide, and titanium dioxide.
准确称取计算所得的氧化镁、氧化铜和二氧化钛的质量,并对它们进行初步的混合,然后缓慢加入回收的酸处理后的磷酸溶液,并加入适量的蒸馏水混合均匀,使其呈现泥浆状态;混合均匀后将混合物在200℃下加热处理24小时,混合物水分蒸干成结块的泥料,然后将泥料粉碎并充分混合,得到玻璃配合料。将玻璃配合料装入氧化铝坩埚中,并在诺巴迪高温升降炉中对玻璃配合料进行高温熔融,熔融过程是:以5℃/min的升温速率,将温度从室温升到1350℃,然后在1350℃保温1小时,以此使得配合料完全熔融,得到玻璃熔体。高温熔融结束后,将玻璃熔体快速倒入水中,进行水淬。收集水淬后的玻璃料,干燥,此样品即为母体玻璃。Accurately weigh the calculated masses of magnesium oxide, copper oxide and titanium dioxide, and mix them initially, then slowly add the recovered acid-treated phosphoric acid solution, and add an appropriate amount of distilled water and mix evenly to make it appear in a slurry state; After mixing evenly, the mixture is heated at 200°C for 24 hours. The mixture is evaporated to dryness and becomes agglomerated mud. The mud is then crushed and thoroughly mixed to obtain a glass batch. Put the glass batch material into an alumina crucible, and perform high-temperature melting of the glass batch material in the Nobadi high-temperature lifting furnace. The melting process is: raising the temperature from room temperature to 1350°C at a heating rate of 5°C/min. , and then kept at 1350°C for 1 hour to completely melt the batch materials and obtain a glass melt. After the high-temperature melting is completed, the glass melt is quickly poured into water for water quenching. Collect the water-quenched glass frit and dry it. This sample is the parent glass.
2.热处理玻璃的制备2. Preparation of heat-treated glass
使用HCT-4型综合热分析仪对母体玻璃进行DTA测试,得到母体玻璃的DTA曲线(见图1)。然后将一定量的步骤1中的母体玻璃以5℃/min的升温速率升至其玻璃转变温度(610℃)热处理1小时,然后以5℃/min的升温速率继续升温至玻璃第一析晶峰温度(698℃)热处理2小时,然后随炉冷却,得到热处理玻璃。Use the HCT-4 comprehensive thermal analyzer to conduct DTA testing on the parent glass, and obtain the DTA curve of the parent glass (see Figure 1). Then heat a certain amount of the parent glass in step 1 to its glass transition temperature (610°C) at a temperature rise rate of 5°C/min for 1 hour, and then continue to heat it up to the first crystallization of the glass at a temperature rise rate of 5°C/min. Heat treatment at the peak temperature (698°C) for 2 hours, and then cool with the furnace to obtain heat-treated glass.
3.多孔材料的制备3. Preparation of porous materials
将一定量的步骤2中的热处理玻璃和3mol/L的磷酸溶液按照1g:100ml的比例加入烧杯中,使用三层聚乙烯薄膜将烧杯口密封,然后将烧杯放入100℃的烘干箱中酸处理48h。酸处理结束后,将磷酸溶液倒出并将其回收,然后使用与磷酸溶液等体积的蒸馏水浸泡玻璃样品2小时,然后使用蒸馏水冲洗玻璃样品3次,烘干后得到多孔材料样品。Add a certain amount of the heat-treated glass in step 2 and 3mol/L phosphoric acid solution into the beaker at the ratio of 1g:100ml, seal the mouth of the beaker with three layers of polyethylene film, and then put the beaker into a drying oven at 100°C Acid treatment for 48h. After the acid treatment, pour out the phosphoric acid solution and recover it, then soak the glass sample with an equal volume of distilled water as the phosphoric acid solution for 2 hours, then rinse the glass sample with distilled water three times, and dry it to obtain a porous material sample.
对所得多孔材料进行XRD分析,结果显示多孔材料晶相同样以MgTi4(PO4)6为主晶相,含有锐钛型TiO2晶相(见图2)。样品的SEM图像如图3所示,可以看出样品表面同样生长着大量纳米片,纳米片相互连接构成了多孔结构,纳米片比实施例1样品的纳米片更薄。该样品的N2吸附等温曲线呈现出明显的Ⅳ型吸附等温线,具有H3型回滞环,表明样品同样是介孔结构,孔径多分布在2-30nm之间(见图5),样品表面积和孔容分别达到了34.18m2/g,0.099cm3/g,该样品的表面积和孔容均较实施例1中利用磷酸直接配料时所得样品的表面积(16.77 m2.g-1)和孔容(0.074 cm3.g-1)增大,有助于对染料的吸附,为后续光催化提供便利。XRD analysis of the obtained porous material showed that the crystal phase of the porous material is also dominated by MgTi 4 (PO 4 ) 6 and contains anatase TiO 2 crystal phase (see Figure 2). The SEM image of the sample is shown in Figure 3. It can be seen that a large number of nanosheets are also grown on the surface of the sample. The nanosheets are connected to each other to form a porous structure. The nanosheets are thinner than the nanosheets of the sample in Example 1. The N 2 adsorption isotherm curve of this sample shows an obvious type IV adsorption isotherm with an H3 type hysteresis loop, indicating that the sample also has a mesoporous structure, with pore diameters mostly distributed between 2-30nm (see Figure 5), and the sample surface area The surface area and pore volume of this sample reached 34.18m 2 /g and 0.099cm 3 /g respectively. The surface area and pore volume of this sample are both higher than the surface area (16.77 m 2. g -1 ) and pore volume of the sample obtained when phosphoric acid was directly batched in Example 1. (0.074 cm 3. g -1 ) increases, which facilitates the adsorption of dyes and facilitates subsequent photocatalysis.
将所得多孔材料在750℃的高温下煅烧0.5h,其SEM图如图4所示,可见煅烧后的样品依然保持着原有的多孔结构,且纳米片表面变得粗糙,部分纳米片上出现新的孔道。The obtained porous material was calcined at a high temperature of 750°C for 0.5 h. The SEM image is shown in Figure 4. It can be seen that the calcined sample still maintains the original porous structure, and the surface of the nanosheets becomes rough, and new particles appear on some nanosheets. of holes.
使用回收的酸处理后的磷酸溶液再次进行玻璃熔体的合成,极大的减少了酸性废液回收处理所产生的高额费用,实现了材料的循环利用;同时所得材料功能晶相与实施例1相同,但其纳米片数量更多更薄,表面积更大,这对于提高材料性能而言无疑是有利的。The recovered acid-treated phosphoric acid solution is used to synthesize the glass melt again, which greatly reduces the high cost of recycling the acidic waste liquid and realizes the recycling of materials; at the same time, the functional crystal phase of the obtained material is consistent with the embodiment 1, but its nanosheets are more numerous, thinner, and have a larger surface area, which is undoubtedly beneficial for improving material performance.
对比例Comparative ratio
按照实施例1的方法得到热处理玻璃,将热处理玻璃和3mol/L的盐酸溶液按照1g:100ml的比例加入烧杯中,使用三层聚乙烯薄膜将烧杯口密封,然后将烧杯放入100℃的烘干箱中分别酸处理13h、48h。酸处理结束后,将盐酸溶液倒出,然后使用与盐酸溶液等体积的蒸馏水浸泡玻璃样品2小时,然后使用蒸馏水冲洗玻璃样品3次,烘干后得到多孔材料样品。其中酸处理13h的样品为对比例1,酸处理48h的样品为对比例2。Obtain heat-treated glass according to the method of Example 1. Add the heat-treated glass and 3 mol/L hydrochloric acid solution into a beaker at a ratio of 1g:100ml. Use a three-layer polyethylene film to seal the mouth of the beaker, and then place the beaker into a 100°C oven. Acid treatment in dry box for 13h and 48h respectively. After the acid treatment, pour out the hydrochloric acid solution, soak the glass sample with an equal volume of distilled water as the hydrochloric acid solution for 2 hours, rinse the glass sample with distilled water three times, and dry it to obtain a porous material sample. The sample treated with acid for 13 hours is Comparative Example 1, and the sample treated with acid for 48 hours is Comparative Example 2.
对所得多孔材料进行XRD分析,结果显示对比例1和2的样品只含有一种光催化功能晶相,即锐钛型TiO2为主晶相,同时还含有Ti(HPO4)2•2H2O晶相(见图2)。样品的SEM图像如图3所示,可以看出样品表面生长着大量纳米片,同时纳米片相互之间连接构成了多孔结构。XRD analysis of the obtained porous materials showed that the samples of Comparative Examples 1 and 2 only contained one photocatalytic functional crystal phase, namely anatase TiO 2 as the main crystal phase, and also contained Ti(HPO 4 ) 2• 2H 2 O crystal phase (see Figure 2). The SEM image of the sample is shown in Figure 3. It can be seen that a large number of nanosheets grow on the surface of the sample, and the nanosheets are connected to each other to form a porous structure.
将对比例1的多孔材料在750℃的高温下煅烧0.5h,然后对煅烧后的样品进行SEM分析,结果如图4所示,从图中可以看出,煅烧后,由于Ti(HPO4)2•2H2O晶相的分解,构成多孔结构的纳米片完全坍塌,孔道消失。孔道消失后会导致多孔材料的比表面积和孔容大大降低,影响其应用。The porous material of Comparative Example 1 was calcined at a high temperature of 750°C for 0.5 h, and then the calcined sample was subjected to SEM analysis. The results are shown in Figure 4. It can be seen from the figure that after calcining, due to Ti(HPO 4 ) With the decomposition of the 2• 2H 2 O crystal phase, the nanosheets constituting the porous structure completely collapse and the pores disappear. The disappearance of pore channels will cause the specific surface area and pore volume of porous materials to be greatly reduced, affecting its application.
应用例Application examples
为了验证本发明制备的多孔材料的性能,下面选取实施例2和对比例2制备的样品进行吸附和光催化降解有机染料亚甲基蓝溶液的实验。利用分光光度计在波长665 nm处测定多孔材料吸附及光催化降解亚甲基蓝溶液前后的吸光度,根据标准曲线计算溶液中亚甲基蓝的浓度。实验过程如下:In order to verify the performance of the porous material prepared by the present invention, the samples prepared in Example 2 and Comparative Example 2 are selected below to conduct experiments on adsorption and photocatalytic degradation of organic dye methylene blue solution. A spectrophotometer was used to measure the absorbance of the methylene blue solution before and after the porous material adsorbed and photocatalytically degraded the methylene blue solution at a wavelength of 665 nm, and the concentration of methylene blue in the solution was calculated based on the standard curve. The experimental process is as follows:
取50mg实施例2和对比例2制备的产品(研磨过50~140目的标准筛),分别将其置于50mL浓度为10mg/L的亚甲基蓝溶液中,先在黑暗条件下搅拌吸附,直至样品达到吸附平衡。在样品达到吸附平衡后,打开紫外灯(300W)照射,继续进行磁力搅拌,从而使得样品在光照条件下,对溶液中的亚甲基蓝分子进行降解。样品对亚甲基蓝溶液中亚甲基蓝的吸附效率,按公式计算。式中,At为在时间为t时的吸附效率,C0为原始溶液的浓度,Ct为溶液在时间为t时的浓度。Take 50 mg of the products prepared in Example 2 and Comparative Example 2 (ground through a standard sieve of 50 to 140 mesh), and place them in 50 mL of a methylene blue solution with a concentration of 10 mg/L. Stir and adsorb under dark conditions until the sample reaches adsorption equilibrium. After the sample reaches adsorption equilibrium, turn on the UV lamp (300W) for irradiation and continue magnetic stirring, so that the sample can degrade the methylene blue molecules in the solution under light conditions. The adsorption efficiency of the sample to methylene blue in the methylene blue solution, according to the formula calculate. In the formula, A t is the adsorption efficiency at time t, C 0 is the concentration of the original solution, and C t is the concentration of the solution at time t.
结果显示,在黑暗条件下搅拌1.5小时后,实施例2和对比例2产品对亚甲基蓝溶液均达到了吸附平衡,吸附率分别是52.04%和47.2%,实施例2样品的吸附效果优于对比例2。在紫外灯照射下搅拌6.5小时后,实施例2和对比例2产品中亚甲基蓝溶液均接近于澄清溶液,实施例2和对比例2产品对亚甲基蓝染料分子的总降解率类似,分别为95.43%和95.87%。The results show that after stirring for 1.5 hours under dark conditions, the products of Example 2 and Comparative Example 2 both reached adsorption equilibrium for the methylene blue solution, and the adsorption rates were 52.04% and 47.2% respectively. The adsorption effect of the Example 2 sample was better than that of the Comparative Example. 2. After stirring under UV lamp irradiation for 6.5 hours, the methylene blue solutions in the products of Example 2 and Comparative Example 2 were both close to clear solutions. The total degradation rates of methylene blue dye molecules in the products of Example 2 and Comparative Example 2 were similar, which were 95.43% and 95.43% respectively. 95.87%.
以上所述仅为本申请的优选实施例而已,并不用于限制本申请,对于本领域的技术人员来说,本申请可以有各种更改和变化。凡在本申请的精神和原则之内,所作的任何修改、等同替换、改进等,均应包含在本申请的保护范围之内。The above descriptions are only preferred embodiments of the present application and are not intended to limit the present application. For those skilled in the art, the present application may have various modifications and changes. Any modifications, equivalent replacements, improvements, etc. made within the spirit and principles of this application shall be included in the protection scope of this application.
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