CN117205940A - A CrMnCoLDH-H catalyst and its preparation method and application - Google Patents
A CrMnCoLDH-H catalyst and its preparation method and application Download PDFInfo
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Abstract
本发明提供了一种CrMnCoLDH‑H催化剂及其制备方法与应用,旨在提供一种对甲醛具有较高的氧化性能的三元水滑石催化剂;其制备方法简单、容易操作,易于批量化生产;Cr0.2MnCo‑LDH的准备方法是:1)分别配制锰盐,记为溶液a;配制钴盐记为溶液b;配制铬盐,记为溶液c;2)将氢氧化钠和碳酸钠配制碱溶液d;3)将溶液a、溶液b、溶液c和溶液d加入到聚四氟乙烯内衬水热釜中,水热釜放入电热恒温鼓风干燥箱中晶化;4)反应结束后冷却至室温,将内衬里的反应物离心,洗涤,最后干燥得到固体产物Cr0.2MnCo‑LDH;5)在含5%H2的H2/Ar混合气中进一步还原,得样品;属于热催化材料和环境保护技术领域。
The invention provides a CrMnCoLDH-H catalyst and its preparation method and application, aiming to provide a ternary hydrotalcite catalyst with high oxidation performance for formaldehyde; its preparation method is simple, easy to operate, and easy to be produced in batches; The preparation method of Cr 0.2 MnCo-LDH is: 1) Prepare manganese salt separately, recorded as solution a; prepare cobalt salt, recorded as solution b; prepare chromium salt, recorded as solution c; 2) Prepare alkali with sodium hydroxide and sodium carbonate Solution d; 3) Add solution a, solution b, solution c and solution d into a polytetrafluoroethylene-lined hydrothermal kettle, and put the hydrothermal kettle into an electric constant temperature blast drying box for crystallization; 4) After the reaction is completed Cool to room temperature, centrifuge the reactants in the inner lining, wash, and finally dry to obtain the solid product Cr 0.2 MnCo-LDH; 5) Further reduce in a H 2 /Ar gas mixture containing 5% H 2 to obtain a sample; it is a thermal Catalytic materials and environmental protection technology fields.
Description
技术领域Technical field
本发明属于热催化材料和环境保护技术领域,具体涉及一种CrMnCoLDH-H催化剂,本发明还涉及CrMnCoLDH-H催化剂的制备方法,以及CrMnCoLDH-H催化氧化甲醛的方法。The invention belongs to the technical fields of thermocatalytic materials and environmental protection, and specifically relates to a CrMnCoLDH-H catalyst. The invention also relates to a preparation method of the CrMnCoLDH-H catalyst and a method for catalytically oxidizing formaldehyde with CrMnCoLDH-H.
背景技术Background technique
自城市化和工业化开始以来,挥发性有机化合物(VOCs)的排放由于对人体的有害影响而成为人们关注的问题,其中甲醛(HCHO)作为主要的挥发性有机化合物之一,已被列为I类致癌物,必须采取措施减少污染物的排放。室温催化氧化因其效率高、处理过程中无二次污染,可将HCHO完全转化为CO2和H2O,被认为是去除HCHO最有前途的技术之一。Since the beginning of urbanization and industrialization, the emission of volatile organic compounds (VOCs) has become a matter of concern due to its harmful effects on the human body. Among them, formaldehyde (HCHO), as one of the main VOCs, has been listed as I Class carcinogens, measures must be taken to reduce the emission of pollutants. Room temperature catalytic oxidation is considered to be one of the most promising technologies for removing HCHO because of its high efficiency, no secondary pollution during the treatment process, and the ability to completely convert HCHO into CO 2 and H 2 O.
传统降解甲醛催化剂可分为贵金属催化剂和非贵金属催化剂。贵金属催化剂包括但不限于铂(Pt)、钯(Pd)、金(Au)银(Ag)和铷(Rb)。这些金属的低温催化活性好,具有使用寿命长、用量低、防腐等优点。然而,贵金属具有价格昂贵、易烧结、易中毒等缺点,这极大地限制了其实际应用。而非贵金属催化剂具有很高的催化活性,并且广泛可用,价格便宜,稳定且耐中毒。这使得它们在HCHO催化氧化中脱颖而出。而开发一种制备方法简单易于实现的非贵金属催化剂来催化氧化甲醛是有很大应用前景的。Traditional formaldehyde degradation catalysts can be divided into precious metal catalysts and non-noble metal catalysts. Precious metal catalysts include, but are not limited to, platinum (Pt), palladium (Pd), gold (Au), silver (Ag), and rubidium (Rb). These metals have good low-temperature catalytic activity and have the advantages of long service life, low dosage, and anti-corrosion. However, precious metals have disadvantages such as being expensive, easy to sinter, and easy to be poisoned, which greatly limits their practical applications. Non-noble metal catalysts, on the other hand, have high catalytic activity and are widely available, cheap, stable and resistant to poisoning. This makes them stand out in HCHO catalytic oxidation. The development of a non-noble metal catalyst with a simple and easy preparation method to catalyze the oxidation of formaldehyde has great application prospects.
LDH(Layered double hydroxides)是一种由带正电荷的金属氢氧化物层和层间填充的带负电荷的阴离子构成的化合物,通式为MII 1-xMIII x(OH)2 z+(An-)z/n·mH2O(MII和MIII分别为二价和三价金属;An-是层间阴离子)。其中阴离子和金属离子可调,具有独特的层状结构,且受晶格定位效应影响,使各金属元素高度分散,作为催化材料得到了广泛的应用。因此我们利用水滑石的定位效应通过水热法合成的第三金属分散的三元催化剂,使催化剂具有较高的甲醛催化效率。LDH (Layered double hydroxides) is a compound composed of a positively charged metal hydroxide layer and negatively charged anions filled between the layers. The general formula is M II 1-x M III x (OH) 2 z+ ( A n- ) z/n ·mH 2 O (M II and M III are divalent and trivalent metals respectively; A n- is an interlayer anion). Among them, the anions and metal ions are adjustable, have a unique layered structure, and are affected by the lattice positioning effect, making each metal element highly dispersed, and have been widely used as catalytic materials. Therefore, we used the positioning effect of hydrotalcite to synthesize a third metal-dispersed three-way catalyst through hydrothermal method, so that the catalyst has high formaldehyde catalytic efficiency.
发明内容Contents of the invention
本发明提供了一种对甲醛具有较高的氧化性能的CrMnCoLDH-H催化剂。The invention provides a CrMnCoLDH-H catalyst with high oxidation performance for formaldehyde.
本发明的第一个目的是提供一种CrMnCoLDH-H催化剂的制备方法,该制备方法简单、容易操作,易于批量化生产。The first object of the present invention is to provide a preparation method of CrMnCoLDH-H catalyst, which is simple, easy to operate and easy to produce in batches.
为此,本发明提供的第一个技术方案是这样的:To this end, the first technical solution provided by the present invention is as follows:
一种CrMnCoLDH-H催化剂的制备方法,包括下述步骤:A preparation method of CrMnCoLDH-H catalyst, including the following steps:
(1)分别配制锰盐,记为溶液a;配制钴盐记为溶液b;配制铬盐,记为溶液c;(1) Prepare manganese salts separately, and record them as solution a; prepare cobalt salts, and record them as solution b; prepare chromium salts, and record them as solution c;
(2)配制氢氧化钠与碳酸钠的混合碱溶液d;(2) Prepare a mixed alkali solution d of sodium hydroxide and sodium carbonate;
(3)将溶液a、溶液b、溶液c和溶液d加入到聚四氟乙烯内衬水热釜中,水热釜放入电热恒温鼓风干燥箱中晶化;(3) Add solution a, solution b, solution c and solution d into a polytetrafluoroethylene-lined hydrothermal kettle, and put the hydrothermal kettle into an electric constant-temperature blast drying box for crystallization;
(4)反应结束后冷却至室温,将内衬里的反应物离心,洗涤,最后干燥得到固体产物Cr0.2MnCo-LDH;(4) After the reaction is completed, cool to room temperature, centrifuge the reactants in the inner lining, wash, and finally dry to obtain the solid product Cr 0.2 MnCo-LDH;
(5)上述固体产物在含5%H2的H2/Ar混合气中,在100-300℃煅烧还原3-10h,所得样品表示为CrMnCoLDH-H;(5) The above solid product is calcined and reduced in a H 2 /Ar gas mixture containing 5% H 2 at 100-300°C for 3-10 hours, and the resulting sample is represented as CrMnCoLDH-H;
在本发明中,所述二价锰盐优选为Mn(acac)2或Mn(NO3)2溶液(50wt.%in H2O),更优选为Mn(NO3)2溶液(50wt.%in H2O);In the present invention, the divalent manganese salt is preferably Mn(acac) 2 or Mn(NO 3 ) 2 solution (50 wt.% in H 2 O), more preferably Mn(NO 3 ) 2 solution (50 wt.% in H 2 O);
钴盐为三价钴盐,所述三价钴盐优选为Co(NO3)2·6H2O或Co(acac)3,更优选为Co(NO3)2·6H2O;The cobalt salt is a trivalent cobalt salt, and the trivalent cobalt salt is preferably Co(NO 3 ) 2 ·6H 2 O or Co(acac) 3 , and more preferably Co(NO 3 ) 2 ·6H 2 O;
在本发明中,锰盐、钴盐、铬盐的摩尔比优选为0.5∶1∶0.1-0.5,更优选为0.5∶1∶0.2-0.4。In the present invention, the molar ratio of manganese salt, cobalt salt and chromium salt is preferably 0.5:1:0.1-0.5, more preferably 0.5:1:0.2-0.4.
在本发明中,优选NaOH与NaCO3的摩尔比为1∶0.2-1.2,更优选为NaOH与NaCO3的摩尔比为1∶0.5-0.8。In the present invention, the molar ratio of NaOH to NaCO 3 is preferably 1:0.2-1.2, and more preferably the molar ratio of NaOH to NaCO 3 is 1:0.5-0.8.
在本发明中,优选晶化温度为100-200℃,更优选为120-150℃;优选晶化时间为6-24h,更优选为12-18h;In the present invention, the preferred crystallization temperature is 100-200°C, more preferably 120-150°C; the preferred crystallization time is 6-24h, more preferably 12-18h;
在本发明中,优选洗涤条件为:去离子水洗涤3-5次,乙醇洗涤3-5次,更优选为去离子水洗涤三次,乙醇洗涤三次;干燥温度为60-80℃,干燥时间为10-24h,更优选为干燥温度为60℃,干燥时间为24h。In the present invention, the preferred washing conditions are: washing with deionized water 3-5 times and washing with ethanol 3-5 times, more preferably washing with deionized water three times and washing with ethanol three times; the drying temperature is 60-80°C, and the drying time is 10-24h, more preferably the drying temperature is 60°C and the drying time is 24h.
在本发明中,优选还原温度为100-300℃,升温速率为5℃/min,还原时间为6-12h,更优选为还原温度150-200℃,升温速率为5℃/min,还原时间为6-12h。In the present invention, the preferred reduction temperature is 100-300°C, the heating rate is 5°C/min, and the reduction time is 6-12h. More preferably, the reduction temperature is 150-200°C, the heating rate is 5°C/min, and the reduction time is 6-12h.
本发明的第二个目的是提供上述CrMnCoLDH-H催化剂催化氧化甲醛的应用。The second object of the present invention is to provide the application of the above-mentioned CrMnCoLDH-H catalyst to catalytically oxidize formaldehyde.
本发明所提供的CrMnCoLDH-H催化剂应用于常温热催化领域。所述催化剂对单体小分子有机物都具有一定的催化效能,可用于降解空气中常见的有机污染物;利用上述的CrMnCoLDH-H催化剂催化氧化甲醛的方法,催化条件为:甲醛浓度-30ppm,空速为21,600mL/(g·h),反应温度30℃,反应时间1h,催化剂质量为0.2g。The CrMnCoLDH-H catalyst provided by the invention is used in the field of normal temperature thermal catalysis. The catalyst has a certain catalytic effect on monomer small molecular organic matter and can be used to degrade common organic pollutants in the air; the method of using the above-mentioned CrMnCoLDH-H catalyst to catalyze the oxidation of formaldehyde, the catalytic conditions are: formaldehyde concentration -30ppm, air The speed is 21,600mL/(g·h), the reaction temperature is 30°C, the reaction time is 1h, and the catalyst mass is 0.2g.
相对于现有技术,本发明技术方案取得的有益效果在于:Compared with the existing technology, the beneficial effects achieved by the technical solution of the present invention are:
(1)本发明提供的技术方案原料选择非贵金属,大大降低催化剂制备成本;(1) The technical solution provided by the present invention selects non-noble metals as raw materials, which greatly reduces the cost of catalyst preparation;
(2)本发明提供的技术方案制备的CrMnCoLDH-H通过氢气还原处理提高晶格氧含量,从而提高其氧化甲醛的能力;(2) The CrMnCoLDH-H prepared by the technical solution provided by the present invention increases the lattice oxygen content through hydrogen reduction treatment, thereby improving its ability to oxidize formaldehyde;
(3)本发明提供的技术方案制备成本较低,制备条件简便,操作方便,便于在工业中放大生产。(3) The technical solution provided by the present invention has low preparation cost, simple preparation conditions, convenient operation, and is convenient for large-scale production in industry.
附图说明Description of the drawings
图1是实施例3和对比例1制备的催化剂的X射线晶体衍射图(XRD);Figure 1 is an X-ray crystal diffraction pattern (XRD) of the catalyst prepared in Example 3 and Comparative Example 1;
图2是实施例3制备的Cr0.2MnCoLDH-H3的扫描电镜(SEM);Figure 2 is a scanning electron microscope (SEM) of Cr 0.2 MnCoLDH-H3 prepared in Example 3;
图3是对比例1制备的CrMnCoLDH的扫描电镜(SEM);Figure 3 is a scanning electron microscope (SEM) of CrMnCoLDH prepared in Comparative Example 1;
图4是实施例3和对比例1制备的催化剂的傅里叶变换红外光谱(FTIR);Figure 4 is the Fourier transform infrared spectrum (FTIR) of the catalyst prepared in Example 3 and Comparative Example 1;
具体实施方式Detailed ways
下面结合具体实施方式,对本发明的技术方案做进一步的详细说明,但不构成对本发明的任何限制,任何人在本发明保护范围之内所做的有限次的修改,仍然在本发明的保护范围之内。The technical solution of the present invention will be further described in detail below in conjunction with the specific embodiments, but this does not constitute any limitation on the present invention. A limited number of modifications made by anyone within the protection scope of the present invention will still be within the protection scope of the present invention. within.
实施例1Example 1
本实施例提供的一种三元水滑石催化剂,是通过下述方法制备的:A ternary hydrotalcite catalyst provided in this embodiment is prepared by the following method:
在本发明中,优选晶化温度为100-200℃,更优选为120-150℃;优选晶化时间为6-24h,更优选为8-16h;In the present invention, the preferred crystallization temperature is 100-200°C, more preferably 120-150°C; the preferred crystallization time is 6-24h, more preferably 8-16h;
(1)取5mmol Mn(NO3)2溶液(50wt.%in H2O)溶于20mL去离子水中,记为溶液a;取10mmol Co(NO3)2·6H2O溶于20mL去离子水中,记为溶液b;2mmol Cr(acac)3加入到20mL去离子水中,记为溶液c;(1) Take 5mmol Mn(NO 3 ) 2 solution (50wt.% in H 2 O) and dissolve it in 20mL deionized water, recorded as solution a; take 10mmol Co(NO 3 ) 2 ·6H 2 O and dissolve it in 20mL deionized water. In water, it is recorded as solution b; 2mmol Cr(acac) 3 is added to 20mL of deionized water, and it is recorded as solution c;
(2)取20mmol NaOH和10mmol Na2CO3加入20mL去离子水中,记为混合碱溶液d;(2) Add 20mmol NaOH and 10mmol Na 2 CO 3 to 20mL of deionized water, and record it as mixed alkali solution d;
(3)将溶液a、溶液b、溶液c和溶液d加入到聚四氟乙烯内衬水热釜中,水热釜放入120℃电热恒温鼓风干燥箱中晶化8h;(3) Add solution a, solution b, solution c and solution d into a polytetrafluoroethylene-lined hydrothermal kettle, and place the hydrothermal kettle into a 120°C electric constant-temperature blast drying oven for crystallization for 8 hours;
(4)反应结束后冷却至室温,将反应物离心,去离子水洗涤3次,乙醇洗涤3次至上清液的pH值为中性,沉淀物在60℃的烘箱中干燥24h得到固体产物Cr0.2MnCoLDH;(4) After the reaction is completed, cool to room temperature, centrifuge the reactant, wash 3 times with deionized water and 3 times with ethanol until the pH value of the supernatant is neutral, and dry the precipitate in an oven at 60°C for 24 hours to obtain the solid product Cr 0.2MnCoLDH ;
(5)上述固体产物在5%H2/Ar混合气氛下150℃煅烧6h,所得样品表示为Cr0.2MnCoLDH-H1。(5) The above solid product is calcined at 150°C for 6 hours in a 5% H 2 /Ar mixed atmosphere, and the resulting sample is represented as Cr 0.2 MnCoLDH-H1.
实施例2Example 2
本实施例提供的另一种三元水滑石催化剂,是通过下述方法制备的:Another ternary hydrotalcite catalyst provided in this embodiment is prepared by the following method:
(1)取5mmol Mn(NO3)2溶液(50wt.%in H2O)溶于20mL去离子水中,记为溶液a;取10mmol Co(NO3)2·6H2O溶于20mL去离子水中,记为溶液b;3mmol Cr(acac)3加入到20mL去离子水中,记为溶液c;(1) Take 5mmol Mn(NO 3 ) 2 solution (50wt.% in H 2 O) and dissolve it in 20mL deionized water, recorded as solution a; take 10mmol Co(NO 3 ) 2 ·6H 2 O and dissolve it in 20mL deionized water. In water, it is recorded as solution b; 3mmol Cr(acac) 3 is added to 20mL of deionized water, and it is recorded as solution c;
(2)取20mmol NaOH和12mmol Na2CO3加入20mL去离子水中,记为混合碱溶液d;(2) Add 20mmol NaOH and 12mmol Na 2 CO 3 to 20mL of deionized water, and record it as mixed alkali solution d;
(3)将溶液a、溶液b、溶液c和溶液d加入到聚四氟乙烯内衬水热釜中,水热釜放入150℃电热恒温鼓风干燥箱中晶化10h;(3) Add solution a, solution b, solution c and solution d into a polytetrafluoroethylene-lined hydrothermal kettle, and place the hydrothermal kettle into a 150°C electric constant-temperature blast drying oven for crystallization for 10 hours;
(4)反应结束后冷却至室温,将反应物离心,去离子水洗涤3次,乙醇洗涤3次至上清液的pH值为中性,沉淀物在60℃的烘箱中干燥24h得到固体产物Cr0.2MnCoLDH;(4) After the reaction is completed, cool to room temperature, centrifuge the reactant, wash 3 times with deionized water and 3 times with ethanol until the pH value of the supernatant is neutral, and dry the precipitate in an oven at 60°C for 24 hours to obtain the solid product Cr 0.2MnCoLDH ;
(5)上述固体产物在5%H2/Ar混合气氛下200℃煅烧6h,所得样品表示为Cr0.3MnCoLDH-H2。(5) The above solid product is calcined at 200°C for 6 hours in a 5% H 2 /Ar mixed atmosphere, and the resulting sample is represented as Cr 0.3 MnCoLDH-H2.
实施例3Example 3
本实施例提供的另一种三元水滑石催化剂,是通过下述方法制备的:Another ternary hydrotalcite catalyst provided in this embodiment is prepared by the following method:
(1)取5mmol Mn(NO3)2溶液(50wt.%in H2O)溶于20mL去离子水中,记为溶液a;取10mmol Co(NO3)2·6H2O溶于20mL去离子水中,记为溶液b;2mmol Cr(NO3)3·9H2O加入到20mL去离子水中,记为溶液c;(1) Take 5mmol Mn(NO 3 ) 2 solution (50wt.% in H 2 O) and dissolve it in 20mL deionized water, recorded as solution a; take 10mmol Co(NO 3 ) 2 ·6H 2 O and dissolve it in 20mL deionized water. in water, recorded as solution b; 2mmol Cr(NO 3 ) 3 ·9H 2 O was added to 20 mL of deionized water, recorded as solution c;
(2)取20mmol NaOH和14mmol Na2CO3加入20mL去离子水中,记为混合碱溶液d;(2) Add 20mmol NaOH and 14mmol Na 2 CO 3 to 20mL of deionized water, and record it as mixed alkali solution d;
(3)将溶液a、溶液b、溶液c和溶液d加入到聚四氟乙烯内衬水热釜中,水热釜放入130℃电热恒温鼓风干燥箱中晶化12h;(3) Add solution a, solution b, solution c and solution d into a polytetrafluoroethylene-lined hydrothermal kettle, and put the hydrothermal kettle into a 130°C electric constant-temperature blast drying oven for crystallization for 12 hours;
(4)反应结束后冷却至室温,将反应物离心,去离子水洗涤3次,乙醇洗涤3次至上清液的pH值为中性,沉淀物在60℃的烘箱中干燥24h得到固体产物Cr0.2MnCoLDH;(4) After the reaction is completed, cool to room temperature, centrifuge the reactant, wash 3 times with deionized water and 3 times with ethanol until the pH value of the supernatant is neutral, and dry the precipitate in an oven at 60°C for 24 hours to obtain the solid product Cr 0.2MnCoLDH ;
(5)上述固体产物在5%H2/Ar混合气氛下200℃煅烧6h,所得样品表示为Cr0.2MnCoLDH-H3;其X射线晶体衍射图(XRD)参阅图1;扫描电镜(SEM)图参阅图2;傅里叶变换红外光谱(FTIR)参阅图4。(5) The above solid product is calcined at 200°C for 6 hours in a 5% H 2 /Ar mixed atmosphere. The obtained sample is represented as Cr 0.2 MnCoLDH-H3; its X-ray crystal diffraction pattern (XRD) is shown in Figure 1; scanning electron microscope (SEM) picture See Figure 2; Fourier transform infrared spectrum (FTIR) see Figure 4.
实施例4Example 4
本实施例提供的另一种三元水滑石催化剂,是通过下述方法制备的:Another ternary hydrotalcite catalyst provided in this embodiment is prepared by the following method:
(1)取5mmol Mn(NO3)2溶液(50wt.%in H2O)溶于20mL去离子水中,记为溶液a;取10mmol Co(NO3)2·6H2O溶于20mL去离子水中,记为溶液b;3mmol Cr(NO3)3·9H2O加入到20mL去离子水中,记为溶液c;(1) Take 5mmol Mn(NO 3 ) 2 solution (50wt.% in H 2 O) and dissolve it in 20mL deionized water, recorded as solution a; take 10mmol Co(NO 3 ) 2 ·6H 2 O and dissolve it in 20mL deionized water. in water, recorded as solution b; 3mmol Cr(NO 3 ) 3 ·9H 2 O was added to 20 mL of deionized water, recorded as solution c;
(2)取20mmol NaOH和16mmol Na2CO3加入20mL去离子水中,记为混合碱溶液d;(2) Add 20mmol NaOH and 16mmol Na 2 CO 3 to 20mL of deionized water, and record it as mixed alkali solution d;
(3)将溶液a、溶液b、溶液c和溶液d加入到聚四氟乙烯内衬水热釜中,水热釜放入140℃电热恒温鼓风干燥箱中晶化14h;(3) Add solution a, solution b, solution c and solution d into a polytetrafluoroethylene-lined hydrothermal kettle, and put the hydrothermal kettle into a 140°C electric constant-temperature blast drying oven for crystallization for 14 hours;
(4)反应结束后冷却至室温,将反应物离心,去离子水洗涤3次,乙醇洗涤3次至上清液的pH值为中性,沉淀物在60℃的烘箱中干燥24h得到固体产物Cr0.2MnCoLDH;(4) After the reaction is completed, cool to room temperature, centrifuge the reactant, wash 3 times with deionized water and 3 times with ethanol until the pH value of the supernatant is neutral, and dry the precipitate in an oven at 60°C for 24 hours to obtain the solid product Cr 0.2MnCoLDH ;
(5)上述固体产物在5%H2/Ar混合气氛下150℃煅烧8h,所得样品表示为Cr0.3MnCoLDH-H4。(5) The above solid product is calcined at 150°C for 8 hours in a 5% H 2 /Ar mixed atmosphere, and the resulting sample is represented as Cr 0.3 MnCoLDH-H4.
实施例5Example 5
本实施例提供的另一种三元水滑石催化剂,是通过下述方法制备的:Another ternary hydrotalcite catalyst provided in this embodiment is prepared by the following method:
(1)取5mmol Mn(NO3)2溶液(50wt.%in H2O)溶于20mL去离子水中,记为溶液a;取10mmol Co(NO3)2·6H2O溶于20mL去离子水中,记为溶液b;4mmol Cr(NO3)3·9H2O加入到20mL去离子水中,记为溶液c;(1) Take 5mmol Mn(NO 3 ) 2 solution (50wt.% in H 2 O) and dissolve it in 20mL deionized water, recorded as solution a; take 10mmol Co(NO 3 ) 2 ·6H 2 O and dissolve it in 20mL deionized water. in water, recorded as solution b; 4mmol Cr(NO 3 ) 3 ·9H 2 O was added to 20 mL of deionized water, recorded as solution c;
(2)取20mmol NaOH和10mmol Na2CO3加入20mL去离子水中,记为混合碱溶液d;(2) Add 20mmol NaOH and 10mmol Na 2 CO 3 to 20mL of deionized water, and record it as mixed alkali solution d;
(3)将溶液a、溶液b、溶液c和溶液d加入到聚四氟乙烯内衬水热釜中,水热釜放入150℃电热恒温鼓风干燥箱中晶化16h;(3) Add solution a, solution b, solution c and solution d into a polytetrafluoroethylene-lined hydrothermal kettle, and put the hydrothermal kettle into a 150°C electric constant-temperature blast drying oven for crystallization for 16 hours;
(4)反应结束后冷却至室温,将反应物离心,去离子水洗涤3次,乙醇洗涤3次至上清液的pH值为中性,沉淀物在60℃的烘箱中干燥24h得到固体产物Cr0.2MnCoLDH;(4) After the reaction is completed, cool to room temperature, centrifuge the reactant, wash 3 times with deionized water and 3 times with ethanol until the pH value of the supernatant is neutral, and dry the precipitate in an oven at 60°C for 24 hours to obtain the solid product Cr 0.2MnCoLDH ;
(5)上述固体产物在5%H2/Ar混合气氛下200℃煅烧8h,所得样品表示为Cr0.4MnCoLDH-H5。(5) The above solid product is calcined at 200°C for 8 hours in a 5% H 2 /Ar mixed atmosphere, and the resulting sample is represented as Cr 0.4 MnCoLDH-H5.
对比例1Comparative example 1
本案例提供的一种三元水滑石催化剂,是通过下述方法制备的:The ternary hydrotalcite catalyst provided in this case is prepared by the following method:
(1)取5mmol Mn(NO3)2溶液(50wt.%in H2O)溶于20mL去离子水中,记为溶液a;取10mmol Co(NO3)2·6H2O溶于20mL去离子水中,记为溶液b;2mmol Cr(NO3)3·9H2O加入到20mL去离子水中,记为溶液c;(1) Take 5mmol Mn(NO 3 ) 2 solution (50wt.% in H 2 O) and dissolve it in 20mL deionized water, recorded as solution a; take 10mmol Co(NO 3 ) 2 ·6H 2 O and dissolve it in 20mL deionized water. in water, recorded as solution b; 2mmol Cr(NO 3 ) 3 ·9H 2 O was added to 20 mL of deionized water, recorded as solution c;
(2)取20mmol NaOH和10mmol Na2CO3加入20mL去离子水中,记为混合碱溶液d;(2) Add 20mmol NaOH and 10mmol Na 2 CO 3 to 20mL of deionized water, and record it as mixed alkali solution d;
(3)将溶液a、溶液b、溶液c和溶液d加入到聚四氟乙烯内衬水热釜中,水热釜放入150℃电热恒温鼓风干燥箱中晶化16h;(3) Add solution a, solution b, solution c and solution d into a polytetrafluoroethylene-lined hydrothermal kettle, and put the hydrothermal kettle into a 150°C electric constant-temperature blast drying oven for crystallization for 16 hours;
(4)反应结束后冷却至室温,将反应物离心,去离子水洗涤3次,乙醇洗涤3次至上清液的pH值为中性,沉淀物在60℃的烘箱中干燥24h得到固体产物Cr0.2MnCoLDH;X射线晶体衍射图(XRD)参阅图1;扫描电镜(SEM)图参阅图3;傅里叶变换红外光谱(FTIR)参阅图4。(4) After the reaction is completed, cool to room temperature, centrifuge the reactant, wash 3 times with deionized water and 3 times with ethanol until the pH value of the supernatant is neutral, and dry the precipitate in an oven at 60°C for 24 hours to obtain the solid product Cr 0.2 MnCoLDH; see Figure 1 for the X-ray crystal diffraction pattern (XRD); see Figure 3 for the scanning electron microscope (SEM) pattern; see Figure 4 for the Fourier transform infrared spectrum (FTIR).
为了更好地证明本申请提供的技术方案的优点,下面给出本申请实施例1至实施例5、对比例1提供的三元水滑石催化剂催化氧化甲醛的活性评价结果。In order to better prove the advantages of the technical solution provided by this application, the activity evaluation results of the ternary hydrotalcite catalyst provided in Examples 1 to 5 and Comparative Example 1 of this application for the catalytic oxidation of formaldehyde are given below.
反应条件:Reaction conditions:
温度:30℃Temperature: 30℃
甲醛浓度:30ppmFormaldehyde concentration: 30ppm
空速:21,600mL/(g.h)Airspeed: 21,600mL/(g.h)
反应稳定时间:1hReaction stabilization time: 1h
催化剂质量:0.2gCatalyst mass: 0.2g
表1CrMnCoLDH催化剂的活性评价结果Table 1 Activity evaluation results of CrMnCoLDH catalyst
从上表可以看出,实施例中CrMnCoLDH-H催化剂均经过氢气还原处理,对比例中催化剂未经氢气还原处理。从表中可以看出,对比例中Cr含量选择实施例中最好的比例0.5∶1∶0.2,发现对比例催化甲醛的转化率明显低于实施例;这说明,氢气还原处理使CrMnCoLDH-H具有良好的甲醛催化活性。因此,实施例是一类活性优良的热催化剂。As can be seen from the above table, the CrMnCoLDH-H catalysts in the examples have all undergone hydrogen reduction treatment, while the catalysts in the comparative examples have not been subjected to hydrogen reduction treatment. As can be seen from the table, the Cr content in the comparative example is the best ratio of 0.5:1:0.2 in the example. It is found that the conversion rate of formaldehyde catalyzed in the comparative example is significantly lower than that in the example; this shows that the hydrogen reduction treatment makes CrMnCoLDH-H Has good formaldehyde catalytic activity. Therefore, the embodiment is a type of thermal catalyst with excellent activity.
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CN118719111A (en) * | 2024-06-07 | 2024-10-01 | 南京大学 | A FeCoMn/g-C3N4 catalyst and its preparation method and application |
Citations (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20040141907A1 (en) * | 2001-04-19 | 2004-07-22 | Max Eisgruber | Method for producing hydrotalcites |
CN105460900A (en) * | 2015-12-07 | 2016-04-06 | 北京化工大学 | Clean preparation method of LDH (layered double hydroxides) |
EP3015429A1 (en) * | 2014-10-30 | 2016-05-04 | Wintershall Holding GmbH | Monolayer from at least one layered double hydroxide (LDH) |
CN110538652A (en) * | 2018-12-21 | 2019-12-06 | 天津大学 | A kind of hydrotalcite-like material with sheet-shaped hierarchical porous structure, preparation method of catalyst and application of the catalyst in propane dehydrogenation |
CN110538648A (en) * | 2018-12-21 | 2019-12-06 | 天津大学 | A kind of flower-shaped hierarchical pore structure hydrotalcite-like material, preparation method of catalyst and application of the catalyst in propane dehydrogenation |
CN111097422A (en) * | 2019-12-09 | 2020-05-05 | 广东省石油与精细化工研究院 | Catalyst for removing formaldehyde and preparation method and application thereof |
CN113181954A (en) * | 2021-04-23 | 2021-07-30 | 北京理工大学 | ZSM-5 molecular sieve nanosheet/LDHs composite catalytic material and preparation method thereof |
CN115445635A (en) * | 2022-09-26 | 2022-12-09 | 江苏中江材料技术研究院有限公司 | Ternary hydrotalcite catalyst and preparation method and application thereof |
CN115487826A (en) * | 2022-09-26 | 2022-12-20 | 江苏中江材料技术研究院有限公司 | Silver-doped manganese-cobalt hydrotalcite catalyst, preparation method thereof and method for degrading formaldehyde |
-
2023
- 2023-10-11 CN CN202311312254.2A patent/CN117205940A/en active Pending
Patent Citations (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20040141907A1 (en) * | 2001-04-19 | 2004-07-22 | Max Eisgruber | Method for producing hydrotalcites |
EP3015429A1 (en) * | 2014-10-30 | 2016-05-04 | Wintershall Holding GmbH | Monolayer from at least one layered double hydroxide (LDH) |
CN105460900A (en) * | 2015-12-07 | 2016-04-06 | 北京化工大学 | Clean preparation method of LDH (layered double hydroxides) |
CN110538652A (en) * | 2018-12-21 | 2019-12-06 | 天津大学 | A kind of hydrotalcite-like material with sheet-shaped hierarchical porous structure, preparation method of catalyst and application of the catalyst in propane dehydrogenation |
CN110538648A (en) * | 2018-12-21 | 2019-12-06 | 天津大学 | A kind of flower-shaped hierarchical pore structure hydrotalcite-like material, preparation method of catalyst and application of the catalyst in propane dehydrogenation |
CN111097422A (en) * | 2019-12-09 | 2020-05-05 | 广东省石油与精细化工研究院 | Catalyst for removing formaldehyde and preparation method and application thereof |
CN113181954A (en) * | 2021-04-23 | 2021-07-30 | 北京理工大学 | ZSM-5 molecular sieve nanosheet/LDHs composite catalytic material and preparation method thereof |
CN115445635A (en) * | 2022-09-26 | 2022-12-09 | 江苏中江材料技术研究院有限公司 | Ternary hydrotalcite catalyst and preparation method and application thereof |
CN115487826A (en) * | 2022-09-26 | 2022-12-20 | 江苏中江材料技术研究院有限公司 | Silver-doped manganese-cobalt hydrotalcite catalyst, preparation method thereof and method for degrading formaldehyde |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN118719111A (en) * | 2024-06-07 | 2024-10-01 | 南京大学 | A FeCoMn/g-C3N4 catalyst and its preparation method and application |
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