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CN108325543A - A kind of synthetic method of activated carbon supported petal-shaped silver orthophosphate complex phase catalysis material - Google Patents

A kind of synthetic method of activated carbon supported petal-shaped silver orthophosphate complex phase catalysis material Download PDF

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CN108325543A
CN108325543A CN201810103886.0A CN201810103886A CN108325543A CN 108325543 A CN108325543 A CN 108325543A CN 201810103886 A CN201810103886 A CN 201810103886A CN 108325543 A CN108325543 A CN 108325543A
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activated carbon
silver phosphate
petal
shaped silver
photocatalytic material
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CN108325543B (en
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李锋锋
张明熹
张利芳
陈晨
郑荣翠
王庆辉
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North China University of Science and Technology
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J27/00Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
    • B01J27/14Phosphorus; Compounds thereof
    • B01J27/16Phosphorus; Compounds thereof containing oxygen, i.e. acids, anhydrides and their derivates with N, S, B or halogens without carriers or on carriers based on C, Si, Al or Zr; also salts of Si, Al and Zr
    • B01J27/18Phosphorus; Compounds thereof containing oxygen, i.e. acids, anhydrides and their derivates with N, S, B or halogens without carriers or on carriers based on C, Si, Al or Zr; also salts of Si, Al and Zr with metals other than Al or Zr
    • B01J27/1802Salts or mixtures of anhydrides with compounds of other metals than V, Nb, Ta, Cr, Mo, W, Mn, Tc, Re, e.g. phosphates, thiophosphates
    • B01J27/1817Salts or mixtures of anhydrides with compounds of other metals than V, Nb, Ta, Cr, Mo, W, Mn, Tc, Re, e.g. phosphates, thiophosphates with copper, silver or gold
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J35/00Catalysts, in general, characterised by their form or physical properties
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J35/00Catalysts, in general, characterised by their form or physical properties
    • B01J35/30Catalysts, in general, characterised by their form or physical properties characterised by their physical properties
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J35/00Catalysts, in general, characterised by their form or physical properties
    • B01J35/30Catalysts, in general, characterised by their form or physical properties characterised by their physical properties
    • B01J35/39Photocatalytic properties
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J37/00Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/02Impregnation, coating or precipitation
    • B01J37/0201Impregnation
    • B01J37/0205Impregnation in several steps
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J37/00Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/02Impregnation, coating or precipitation
    • B01J37/0201Impregnation
    • B01J37/0207Pretreatment of the support
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J37/00Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/02Impregnation, coating or precipitation
    • B01J37/0236Drying, e.g. preparing a suspension, adding a soluble salt and drying

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Abstract

本发明涉及一种活性炭负载花瓣状磷酸银复相光催化材料的合成方法,其特征在于:将预处理过的活性炭置于摇床中振荡,振荡过程中,向活性炭表面交替均匀喷洒AgNO3和H3PO4溶液,反复进行5~20次;然后将活性炭取出,清洗、干燥后,得到活性炭负载花瓣状磷酸银复相光催化材料。这种复相材料结合了活性炭的巨大的比表面积和磷酸银优秀的光催化性能,具有更强的有机污染物处理能力,同时相比磷酸银粉体更易回收。The invention relates to a method for synthesizing an activated carbon-loaded petal-shaped silver phosphate composite photocatalytic material, which is characterized in that: the pretreated activated carbon is placed in a shaker for oscillation, and during the oscillation process, AgNO3 and H 3 PO 4 solution, repeated 5 to 20 times; then the activated carbon was taken out, washed and dried to obtain the activated carbon-loaded petal-shaped silver phosphate composite photocatalytic material. This composite material combines the huge specific surface area of activated carbon and the excellent photocatalytic performance of silver phosphate, has a stronger ability to treat organic pollutants, and is easier to recycle than silver phosphate powder.

Description

一种活性炭负载花瓣状磷酸银复相光催化材料的合成方法Synthesis method of activated carbon-loaded petal-shaped silver phosphate composite photocatalytic material

技术领域technical field

本发明涉及一种活性炭负载花瓣状磷酸银复相光催化材料的合成方法,属于无机非金属材料领域。The invention relates to a method for synthesizing an active carbon-loaded petal-shaped silver phosphate composite photocatalytic material, which belongs to the field of inorganic non-metallic materials.

背景技术Background technique

当今社会,由于传统工业的高度发展,传统的化石燃料过度使用,一方面传统能源面临枯竭,另一方面也造成了严重的大气和水体污染。环境污染和传统能源枯竭已经成为人类社会最重要、也是亟待解决的两个问题。为了缓解和解决上述问题,还必须寻找取之方便、用之清洁的新能源,以及对目前已经产生的环境问题加以治理。光催化技术的诞生,使得解决上述问题看到了希望,并有望才能够实现人类社会的健康发展。In today's society, due to the high development of traditional industries and the excessive use of traditional fossil fuels, on the one hand, traditional energy is facing exhaustion, and on the other hand, it has also caused serious air and water pollution. Environmental pollution and the depletion of traditional energy sources have become the two most important problems in human society that need to be solved urgently. In order to alleviate and solve the above problems, it is also necessary to find new energy sources that are easy to obtain and use cleanly, and to control the environmental problems that have occurred so far. The birth of photocatalytic technology has brought hope to solve the above problems, and it is expected to be able to realize the healthy development of human society.

光催化剂可以吸收光能,产生自由电子和空穴,再反应成为活性物种,与反应物进一步反应,由此实现光能向化学能的转化。日本科学家率先研究发现了二氧化钛具有光催化分解水和降解有机污染物的功能。尽管二氧化钛具有高催化活性、良好的化学稳定性等特点,目前也已经有了一定的应用,但是,其仅在紫外光区具有吸收、量子效率不高等劣势确限制着其发展。Photocatalysts can absorb light energy, generate free electrons and holes, and then react to become active species, and further react with reactants, thereby realizing the conversion of light energy into chemical energy. Japanese scientists took the lead in discovering that titanium dioxide has the function of photocatalytically splitting water and degrading organic pollutants. Although titanium dioxide has the characteristics of high catalytic activity and good chemical stability, it has been applied to a certain extent at present, but its disadvantages such as absorption only in the ultraviolet region and low quantum efficiency really limit its development.

光催化领域的研究逐渐将重点转移到可见光催化材料,研究者发现CdS、BiVO4、C3N4、Ag3PO4等窄带隙光催化剂具有较宽的吸收范围,可以被可见光激发。其中Ag3PO4它可以吸收波长小于520nm的太阳光,在多种有机染料降解实验中表现出来了极其优越的光催化活性,其分解水产氧能力也相当可观。Research in the field of photocatalysis has gradually shifted its focus to visible light catalytic materials. Researchers have found that narrow bandgap photocatalysts such as CdS, BiVO 4 , C 3 N 4 , and Ag 3 PO 4 have a wide absorption range and can be excited by visible light. Among them, Ag 3 PO 4 can absorb sunlight with a wavelength of less than 520nm, and has shown extremely superior photocatalytic activity in various organic dye degradation experiments, and its ability to decompose water and produce oxygen is also considerable.

活性炭是一种吸附剂,具有巨大的比表面积和强吸附能力,能够吸附液体或者气体中的有机污染物。Ag3PO4与活性炭复合后,不仅提升了Ag3PO4本身的分散性,而且巨大的表面积使得有机污染物与Ag3PO4的接触更加充分,从而促进光催化反应的进行。Activated carbon is a kind of adsorbent with huge specific surface area and strong adsorption capacity, which can adsorb organic pollutants in liquid or gas. After Ag 3 PO 4 is combined with activated carbon, not only the dispersion of Ag 3 PO 4 itself is improved, but also the huge surface area makes the contact between organic pollutants and Ag 3 PO 4 more sufficient, thus promoting the photocatalytic reaction.

申请号为201310246213.8 的专利报道了一种磷酸银光催化剂的制备方法,所述制备方法,包括如下步骤:在聚乙二醇200中依次加入乙酸银、磷酸水溶液,调节pH至5-6,在搅拌状态下反应;步骤所述反应结束后,离心取沉淀,洗涤,干燥后即得磷酸银光催化剂。采用本发明方法,得到磷酸银光催化剂为新颖的管状微孔结构,其光催化活性较高。申请号为201210341324.2的专利报道了一种可见光驱动的纳米磷酸银催化剂的制备方法,本发明通过使用不同光源照射和微量注射反应物的方法,制备出了可以稳定存在的纳米磷酸银光催化剂,避免了在可见光下制备,产物会发生分解的问题。本方法所制备的磷酸银颗粒为球簇结构,单体直径在20~60nm,整体直径在60~300n,远小于市场上常见的微米级磷酸银。但是,上述案例与本申请不同的是,上述案例都是纯物质磷酸银的制备方法。The patent application number 201310246213.8 reports a preparation method of silver phosphate photocatalyst, the preparation method comprises the following steps: adding silver acetate and phosphoric acid aqueous solution to polyethylene glycol 200 in sequence, adjusting the pH to 5-6, and The reaction is carried out under stirring; after the reaction in the step is completed, the precipitate is collected by centrifugation, washed and dried to obtain the silver phosphate photocatalyst. By adopting the method of the invention, the silver phosphate photocatalyst is obtained as a novel tubular microporous structure, and its photocatalytic activity is relatively high. The patent application number 201210341324.2 reports a preparation method of a visible light-driven nano-silver phosphate catalyst. The present invention prepares a stable nano-silver phosphate photocatalyst by using different light source irradiation and micro-injection of reactants to avoid In addition to the preparation under visible light, the product will decompose. The silver phosphate particles prepared by the method have a spherical cluster structure, the diameter of the monomer is 20-60nm, and the overall diameter is 60-300nm, which is far smaller than the common micron silver phosphate in the market. However, the above-mentioned cases are different from the present application in that the above-mentioned cases are all preparation methods of pure silver phosphate.

申请号为201410001356.7 的专利报道了一种剥离型水滑石负载磷酸银催化剂的制备方法,具体步骤如下:将尿嘧啶溶解在NaOH溶液中,加入硝酸银,搅拌至溶液澄清透明,加入干燥的市售或自制水滑石粉末,搅拌,沉淀分离,烘干;将烘干得到的产品在微波炉中,微波辐照;将微波辐照过的产品加入到磷酸溶液中,搅拌,沉淀分离,烘干即得到一种剥离型水滑石负载磷酸银催化剂。申请号为201410156228.X的专利报道了一种埃洛石负载磷酸银光催化剂的制备方法,具体步骤如下:将埃洛石加入到硝酸溶液中,得到酸处理的埃洛石,将4~8g酸处理的埃洛石置于真空抽滤瓶中,在真空状态下和硝酸银乙醇溶液混合,让硝酸银充分进入埃洛石管内,继续搅拌2~3h,固液分离,真空70~80℃烘干;将烘干得到的产品加入到50mL,浓度为0.5~1.5mol/L的磷酸二氢钠溶液中,搅拌4~5h,固液分离,洗涤,100~105℃烘干即得一种埃洛石负载磷酸银光催化剂。申请号为201410259216.X的专利报道了一种负载型磷酸银光催化剂的制备方法,具体步骤如下:称取研磨后过40目筛的多孔羟基磷灰石80~100g,填充于上下有阀门控制的玻璃管内;分别配制浓度为0.01~0.1mol/L的HNO3溶液、浓度为0.01~0.1mol/L的NaNO3溶液和浓度为0.2~0.8mol/L的AgNO3溶液各200mL;将填充有多孔羟基磷灰石的玻璃管竖直,打开上下阀门,由底部向管内注入HNO3溶液,当溶液能浸没多孔羟基磷灰石后,排出HNO3溶液,保持底部阀门打开,由顶部注入NaNO3溶液,让NaNO3溶液从顶部注入后从底部流出,再关闭底部阀门,从顶部注入AgNO3溶液后浸泡20~30min,将AgNO3溶液从底部放出,玻璃管中的颗粒物经去离子水洗、干燥后即得到一种负载型磷酸银光催化剂。上述案例与本申请都属于负载型磷酸银光催化剂的制备,但是与本申请涉及的载体、负载工艺、磷酸银的尺寸相貌完全不同,最终光催化活性也大有不同。The patent application number 201410001356.7 reports a preparation method of an exfoliated hydrotalcite-supported silver phosphate catalyst. The specific steps are as follows: dissolve uracil in NaOH solution, add silver nitrate, stir until the solution is clear and transparent, add dry commercially available Or self-made hydrotalcite powder, stirred, precipitated and separated, and dried; put the dried product in a microwave oven, and microwave irradiated; added the microwave irradiated product into the phosphoric acid solution, stirred, precipitated and separated, and dried to obtain An exfoliated hydrotalcite-supported silver phosphate catalyst. The patent application number 201410156228.X reports a preparation method of halloysite-loaded silver phosphate photocatalyst, the specific steps are as follows: add halloysite into nitric acid solution to obtain acid-treated halloysite, and mix 4-8g The acid-treated halloysite is placed in a vacuum filter bottle, mixed with silver nitrate ethanol solution in a vacuum state, let the silver nitrate fully enter the halloysite tube, continue to stir for 2-3 hours, separate solid and liquid, vacuum 70-80°C Drying; add the product obtained by drying into 50mL of sodium dihydrogen phosphate solution with a concentration of 0.5-1.5mol/L, stir for 4-5 hours, separate solid and liquid, wash, and dry at 100-105°C to obtain a Halloysite supported silver phosphate photocatalyst. The patent application number 201410259216.X reports a preparation method of a supported silver phosphate photocatalyst. The specific steps are as follows: Weigh 80-100g of porous hydroxyapatite that has been ground and passed through a 40-mesh sieve, and fill it in the top and bottom with valve control. In the glass tube; respectively prepare 200 mL of HNO 3 solution with a concentration of 0.01-0.1 mol/L, NaNO 3 solution with a concentration of 0.01-0.1 mol/L and AgNO 3 solution with a concentration of 0.2-0.8 mol/L; The glass tube of porous hydroxyapatite is vertical, open the upper and lower valves, inject HNO 3 solution into the tube from the bottom, when the solution can immerse the porous hydroxyapatite, discharge the HNO 3 solution, keep the bottom valve open, and inject NaNO 3 from the top solution, let the NaNO 3 solution flow out from the bottom after injecting it from the top, then close the bottom valve, inject the AgNO 3 solution from the top and soak for 20-30 minutes, release the AgNO 3 solution from the bottom, and wash the particles in the glass tube with deionized water and dry Then a loaded silver phosphate photocatalyst is obtained. The above case and this application all belong to the preparation of supported silver phosphate photocatalyst, but the carrier, loading process, and size and appearance of silver phosphate involved in this application are completely different, and the final photocatalytic activity is also very different.

本申请与上述报道不同,本申请通过向活性炭表面反复喷洒AgNO3溶液和H3PO4溶液,获得活性炭负载花瓣状磷酸银复相光催化材料。这种光催化剂在降解有机污染物等领域具有广阔的应用前景。This application is different from the above reports. This application obtains petal-shaped silver phosphate composite photocatalytic material supported by activated carbon by repeatedly spraying AgNO 3 solution and H 3 PO 4 solution on the surface of activated carbon. This photocatalyst has broad application prospects in the field of degradation of organic pollutants.

发明内容Contents of the invention

本发明主要涉及一种活性炭负载花瓣状磷酸银复相光催化材料的合成方法,具体发明内容如下。The invention mainly relates to a synthesis method of a petal-shaped silver phosphate composite photocatalytic material supported by activated carbon, and the specific content of the invention is as follows.

1、称取10~20g活性炭超声清洗、干燥、再于马弗炉中400~500℃煅烧活化1~2h,然后置于摇床中振荡;振荡过程中,先向活性炭表面均匀喷洒3mmol/L 的AgNO3溶液,控制喷洒速度约为5~10mL/min,每次喷洒2min;然后向活性炭表面均匀喷洒1mmol/L 的H3PO4溶液,控制喷洒速度约为5~10mL/min,每次喷洒2min,如此反复进行5~20次;然后将活性炭取出,用去离子水清洗3~5次,干燥后,得到活性炭负载花瓣状磷酸银复相光催化材料。1. Weigh 10~20g of activated carbon, ultrasonically clean it, dry it, then calcinate and activate it in a muffle furnace at 400~500°C for 1~2h, and then place it in a shaking table for oscillation; during the oscillation process, first spray 3mmol/L evenly on the surface of the activated carbon AgNO 3 solution, the control spraying speed is about 5~10mL/min, spraying 2min each time; then evenly spray 1mmol/L H 3 PO 4 solution on the surface of activated carbon, controlling the spraying speed is about 5~10mL/min, each time Spray for 2 minutes, and repeat this process 5 to 20 times; then take out the activated carbon, wash it with deionized water for 3 to 5 times, and dry it to obtain a petal-shaped silver phosphate composite photocatalytic material loaded with activated carbon.

2、超声清洗温度为室温,频率20kHz,功率5kW。2. The ultrasonic cleaning temperature is room temperature, the frequency is 20kHz, and the power is 5kW.

3、负载前活性炭的干燥方式为鼓风烘干,干燥温度100~150℃,干燥时间3~5h。3. The drying method of activated carbon before loading is blast drying, the drying temperature is 100~150℃, and the drying time is 3~5h.

4、摇床振荡的方式为回旋振荡,回旋频率为50~400r/min,振荡幅度为20~30mm。4. The oscillation mode of the shaking table is orbital oscillation, the orbital frequency is 50~400r/min, and the oscillation amplitude is 20~30mm.

5、负载后活性炭的干燥方法为:首先N2吹干5~10min,N2流速为0.2~0.5m3/min;然后再于80~100℃下,真空干燥10~12h,真空度<200Pa。5. The drying method of activated carbon after loading is as follows: first blow dry with N 2 for 5~10min, and the flow rate of N 2 is 0.2~0.5m 3 /min; .

附图说明Description of drawings

图1为以实例1工艺条件下制备出的活性炭负载花瓣状磷酸银复相光催化材料的SEM图。Fig. 1 is the SEM image of the activated carbon-loaded petal-shaped silver phosphate composite photocatalytic material prepared under the process conditions of Example 1.

图2为以实例1工艺条件下制备出的1g质量的活性炭负载花瓣状磷酸银复相光催化材料的对罗丹明B(0.5g/L,400ml)的降解曲线图。Fig. 2 is the degradation curve of Rhodamine B (0.5g/L, 400ml) of 1g mass of activated carbon-loaded petal-shaped silver phosphate composite photocatalytic material prepared under the process conditions of Example 1.

具体实施方式Detailed ways

以下结合实施例对本发明进行详细说明,本发明不受这些制造实施例所限。The present invention will be described in detail below in conjunction with examples, and the present invention is not limited by these examples.

实例1Example 1

称取10g活性炭于室温超声清洗,超声频率20kHz,超声功率5kW,于110℃鼓风干燥3h,再于马弗炉中400℃煅烧活化2h;然后将活性炭置于摇床中振荡,回旋频率为200r/min,振荡幅度为20mm;振荡过程中,先向活性炭表面均匀喷洒3mmol/L 的AgNO3溶液,控制喷洒速度约为5mL/min,每次喷洒2min;然后向活性炭表面均匀喷洒1mmol/L 的H3PO4溶液,控制喷洒速度约为5mL/min,每次喷洒2min,如此反复进行10次;然后将活性炭取出,用去离子水清洗3次;N2吹干5min,N2流速为0.2m3/min;然后再于80℃下真空干燥12h,真空度=180Pa,得到活性炭负载花瓣状磷酸银复相光催化材料。Weigh 10g of activated carbon and ultrasonically clean it at room temperature with an ultrasonic frequency of 20kHz and an ultrasonic power of 5kW, air-dry it at 110°C for 3h, then calcinate and activate it in a muffle furnace at 400°C for 2h; 200r/min, the oscillation amplitude is 20mm; during the oscillation process, first spray 3mmol/L AgNO 3 solution evenly on the surface of the activated carbon, control the spraying speed to about 5mL/min, and spray 2min each time; then spray 1mmol/L evenly on the surface of the activated carbon H 3 PO 4 solution, the spraying speed is controlled to be about 5mL/min, each spraying is 2min, and this is repeated 10 times; then the activated carbon is taken out and washed with deionized water for 3 times; N 2 is blown dry for 5 min, and the flow rate of N 2 is 0.2m 3 /min; and then vacuum-dried at 80°C for 12h, vacuum degree = 180Pa, to obtain petal-shaped silver phosphate multi-phase photocatalytic material supported by activated carbon.

实例2Example 2

称取10g活性炭于室温超声清洗,超声频率20kHz,超声功率5kW,于100℃鼓风干燥4h,再于马弗炉中400℃煅烧活化1h;然后将活性炭置于摇床中振荡,回旋频率为200r/min,振荡幅度为20mm;振荡过程中,先向活性炭表面均匀喷洒3mmol/L 的AgNO3溶液,控制喷洒速度约为7mL/min,每次喷洒2min;然后向活性炭表面均匀喷洒1mmol/L 的H3PO4溶液,控制喷洒速度约为7mL/min,每次喷洒2min,如此反复进行12次;然后将活性炭取出,用去离子水清洗3次;N2吹干10min,N2流速为0.5m3/min;然后再于80℃下真空干燥12h,真空度=150Pa,得到活性炭负载花瓣状磷酸银复相光催化材料。Weigh 10g of activated carbon and ultrasonically clean it at room temperature with an ultrasonic frequency of 20kHz and an ultrasonic power of 5kW, air-dry it at 100°C for 4h, then calcinate and activate it in a muffle furnace at 400°C for 1h; 200r/min, the oscillation amplitude is 20mm; during the oscillation process, first spray 3mmol/L AgNO 3 solution evenly on the surface of the activated carbon, control the spraying speed to about 7mL/min, and spray 2min each time; then spray 1mmol/L evenly on the surface of the activated carbon H 3 PO 4 solution, the spraying speed is controlled to be about 7mL/min, each spraying is 2min, and this is repeated 12 times; then the activated carbon is taken out and washed with deionized water for 3 times; N 2 is blown dry for 10 min, and the flow rate of N 2 is 0.5m 3 /min; then vacuum-dried at 80°C for 12h, vacuum degree = 150Pa, to obtain petal-shaped silver phosphate multi-phase photocatalytic material supported by activated carbon.

实例3Example 3

称取15g活性炭于室温超声清洗,超声频率20kHz,超声功率5kW,于120℃鼓风干燥3h,再于马弗炉中450℃煅烧活化1.5h;然后将活性炭置于摇床中振荡,回旋频率为200r/min,振荡幅度为30mm;振荡过程中,先向活性炭表面均匀喷洒3mmol/L 的AgNO3溶液,控制喷洒速度约为8mL/min,每次喷洒2min;然后向活性炭表面均匀喷洒1mmol/L 的H3PO4溶液,控制喷洒速度约为8mL/min,每次喷洒2min,如此反复进行5次;然后将活性炭取出,用去离子水清洗3次;N2吹干10min,N2流速为0.5m3/min;然后再于90℃下真空干燥10h,真空度=180Pa,得到活性炭负载花瓣状磷酸银复相光催化材料。Weigh 15g of activated carbon and ultrasonically clean it at room temperature with an ultrasonic frequency of 20kHz and an ultrasonic power of 5kW, air-dry it at 120°C for 3h, then calcinate and activate it in a muffle furnace at 450°C for 1.5h; The vibration amplitude is 200r/min, and the oscillation amplitude is 30mm; during the oscillation process, first spray 3mmol/L AgNO 3 solution evenly on the surface of the activated carbon, control the spraying speed to about 8mL/min, and spray 2min each time; then spray 1mmol/L AgNO 3 solution evenly on the surface of the activated carbon L of H 3 PO 4 solution, the spraying speed is controlled to be about 8mL/min, each spraying is 2min, and this is repeated 5 times; then the activated carbon is taken out and washed 3 times with deionized water; 0.5m 3 /min; then vacuum-dried at 90°C for 10h, vacuum degree = 180Pa, to obtain a petal-shaped silver phosphate multi-phase photocatalytic material supported by activated carbon.

实例4Example 4

称取15g活性炭于室温超声清洗,超声频率20kHz,超声功率5kW,于130℃鼓风干燥4h,再于马弗炉中450℃煅烧活化2h;然后将活性炭置于摇床中振荡,回旋频率为200r/min,振荡幅度为25mm;振荡过程中,先向活性炭表面均匀喷洒3mmol/L 的AgNO3溶液,控制喷洒速度约为8mL/min,每次喷洒2min;然后向活性炭表面均匀喷洒1mmol/L 的H3PO4溶液,控制喷洒速度约为8mL/min,每次喷洒2min,如此反复进行10次;然后将活性炭取出,用去离子水清洗3次;N2吹干10min,N2流速为0.5m3/min;然后再于90℃下真空干燥12h,真空度=160Pa,得到活性炭负载花瓣状磷酸银复相光催化材料。Weigh 15g of activated carbon and ultrasonically clean it at room temperature with an ultrasonic frequency of 20kHz and an ultrasonic power of 5kW, air-dry it at 130°C for 4h, then calcinate and activate it in a muffle furnace at 450°C for 2h; 200r/min, the oscillation amplitude is 25mm; during the oscillation process, first spray 3mmol/L AgNO 3 solution evenly on the surface of activated carbon, control the spraying speed to about 8mL/min, spray 2min each time; then spray 1mmol/L evenly on the surface of activated carbon H 3 PO 4 solution, the spraying speed is controlled to be about 8mL/min, each spraying is 2min, and this is repeated 10 times; then the activated carbon is taken out and washed with deionized water for 3 times; N 2 is blown dry for 10 min, and the flow rate of N 2 is 0.5m 3 /min; then vacuum-dried at 90°C for 12h, vacuum degree = 160Pa, to obtain petal-shaped silver phosphate multi-phase photocatalytic material supported by activated carbon.

实例5Example 5

称取15g活性炭于室温超声清洗,超声频率20kHz,超声功率5kW,于120℃鼓风干燥5h,再于马弗炉中500℃煅烧活化1h;然后将活性炭置于摇床中振荡,回旋频率为200r/min,振荡幅度为30mm;振荡过程中,先向活性炭表面均匀喷洒3mmol/L 的AgNO3溶液,控制喷洒速度约为10mL/min,每次喷洒2min;然后向活性炭表面均匀喷洒1mmol/L 的H3PO4溶液,控制喷洒速度约为10mL/min,每次喷洒2min,如此反复进行15次;然后将活性炭取出,用去离子水清洗5次;N2吹干10min,N2流速为0.5m3/min;然后再于100℃下真空干燥10h,真空度=160Pa,得到活性炭负载花瓣状磷酸银复相光催化材料。Weigh 15g of activated carbon and ultrasonically clean it at room temperature with an ultrasonic frequency of 20kHz and an ultrasonic power of 5kW, air-dry it at 120°C for 5h, then calcinate and activate it in a muffle furnace at 500°C for 1h; 200r/min, the oscillation amplitude is 30mm; during the oscillation process, first spray 3mmol/L AgNO 3 solution evenly on the surface of the activated carbon, control the spraying speed to about 10mL/min, and spray 2min each time; then spray 1mmol/L evenly on the surface of the activated carbon H 3 PO 4 solution, the spraying speed is controlled to be about 10mL/min, each spraying is 2min, and this is repeated 15 times; then the activated carbon is taken out and washed 5 times with deionized water; N 2 is blown dry for 10 min, and the flow rate of N 2 is 0.5m 3 /min; then vacuum-dried at 100°C for 10h, vacuum degree = 160Pa, to obtain petal-shaped silver phosphate composite photocatalytic material supported by activated carbon.

实例6Example 6

称取20g活性炭于室温超声清洗,超声频率20kHz,超声功率5kW,于150℃鼓风干燥5h,再于马弗炉中500℃煅烧活化2h;然后将活性炭置于摇床中振荡,回旋频率为300r/min,振荡幅度为30mm;振荡过程中,先向活性炭表面均匀喷洒3mmol/L 的AgNO3溶液,控制喷洒速度约为10mL/min,每次喷洒2min;然后向活性炭表面均匀喷洒1mmol/L 的H3PO4溶液,控制喷洒速度约为10mL/min,每次喷洒2min,如此反复进行20次;然后将活性炭取出,用去离子水清洗5次;N2吹干10min,N2流速为0.5m3/min;然后再于100℃下真空干燥12h,真空度=180Pa,得到活性炭负载花瓣状磷酸银复相光催化材料。Weigh 20g of activated carbon and ultrasonically clean it at room temperature with an ultrasonic frequency of 20kHz and an ultrasonic power of 5kW, air-dry at 150°C for 5h, and then calcinate and activate it in a muffle furnace at 500°C for 2h; 300r/min, the oscillation amplitude is 30mm; during the oscillation process, first spray 3mmol/L AgNO 3 solution evenly on the surface of the activated carbon, control the spraying speed to about 10mL/min, and spray 2min each time; then spray 1mmol/L evenly on the surface of the activated carbon H 3 PO 4 solution, the spraying speed is controlled to be about 10mL/min, each spraying is 2min, and this is repeated 20 times; then the activated carbon is taken out and washed 5 times with deionized water; N 2 is blown dry for 10 min, and the flow rate of N 2 is 0.5m 3 /min; then vacuum-dried at 100°C for 12h, vacuum degree = 180Pa, to obtain a petal-shaped silver phosphate composite photocatalytic material supported on activated carbon.

Claims (5)

1.一种活性炭负载花瓣状磷酸银复相光催化材料的合成方法,其特征在于:称取10~20g活性炭超声清洗、干燥、再于马弗炉中400~500℃煅烧活化1~2h,然后置于摇床中振荡;振荡过程中,先向活性炭表面均匀喷洒3mmol/L 的AgNO3溶液,控制喷洒速度约为5~10mL/min,每次喷洒2min;然后向活性炭表面均匀喷洒1mmol/L 的H3PO4溶液,控制喷洒速度约为5~10mL/min,每次喷洒2min,如此反复进行5~20次;然后将活性炭取出,用去离子水清洗3~5次,干燥后,得到活性炭负载花瓣状磷酸银复相光催化材料。1. A method for synthesizing active carbon-loaded petal-shaped silver phosphate composite photocatalytic materials, characterized in that: 10-20 g of activated carbon is ultrasonically cleaned, dried, and then calcined and activated in a muffle furnace at 400-500 °C for 1-2 hours. Then place it in a shaking table and oscillate; during the oscillating process, spray 3mmol/L AgNO 3 solution evenly on the surface of the activated carbon, control the spraying speed to about 5-10mL/min, and spray 2min each time; then spray 1mmol/L AgNO 3 solution evenly on the surface of the activated carbon. L of H 3 PO 4 solution, control the spraying speed to about 5~10mL/min, spray 2min each time, repeat this way 5~20 times; then take out the activated carbon, wash it with deionized water 3~5 times, after drying, The activated carbon-loaded petal-shaped silver phosphate composite photocatalytic material was obtained. 2.如权利要求1所述一种活性炭负载花瓣状磷酸银复相光催化材料的合成方法,其特征在于超声清洗温度为室温,频率20kHz,功率5kW。2. the synthetic method of a kind of gac-loaded petal-shaped silver phosphate composite photocatalytic material as claimed in claim 1, is characterized in that ultrasonic cleaning temperature is room temperature, frequency 20kHz, power 5kW. 3.如权利要求1所述一种活性炭负载花瓣状磷酸银复相光催化材料的合成方法,其特征在于负载前活性炭的干燥方式为鼓风烘干,干燥温度100~150℃,干燥时间3~5h。3. A kind of synthetic method of activated carbon-loaded petal-shaped silver phosphate composite photocatalytic material as claimed in claim 1, characterized in that the drying method of the activated carbon before loading is blast drying, the drying temperature is 100 ~ 150 ° C, and the drying time is 3 ~5h. 4.如权利要求1所述一种活性炭负载花瓣状磷酸银复相光催化材料的合成方法,其特征在于摇床振荡的方式为回旋振荡,回旋频率为50~400r/min,振荡幅度为20~30mm。4. A kind of synthetic method of active carbon loading petal-shaped silver phosphate composite photocatalytic material as claimed in claim 1, it is characterized in that the mode of shaker oscillation is cyclotron oscillation, and the cyclotron frequency is 50 ~ 400r/min, and the oscillation amplitude is 20 ~30mm. 5.如权利要求1所述一种活性炭负载花瓣状磷酸银复相光催化材料的合成方法,其特征在于负载后活性炭的干燥方法为:首先N2吹干5~10min,N2流速为0.2~0.5m3/min;然后再于80~100℃下,真空干燥10~12h,真空度<200Pa。5. A kind of synthetic method of active carbon loaded petal-shaped silver phosphate composite photocatalytic material as claimed in claim 1, it is characterized in that the drying method of activated carbon after loading is: at first N 2 Dry 5~10min, N Flow rate is 0.2 ~0.5m 3 /min; then vacuum dry at 80~100℃ for 10~12h, vacuum degree <200Pa.
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Denomination of invention: Synthesis method of petal shaped silver phosphate composite photocatalytic material loaded on activated carbon

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