CN108786824A - Si柱撑粘土负载高分散Co3O4-CeO2催化剂的制备方法及应用 - Google Patents

Si柱撑粘土负载高分散Co3O4-CeO2催化剂的制备方法及应用 Download PDF

Info

Publication number
CN108786824A
CN108786824A CN201810485352.9A CN201810485352A CN108786824A CN 108786824 A CN108786824 A CN 108786824A CN 201810485352 A CN201810485352 A CN 201810485352A CN 108786824 A CN108786824 A CN 108786824A
Authority
CN
China
Prior art keywords
spc
catalyst
preparation
ceo
load high
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN201810485352.9A
Other languages
English (en)
Inventor
左树锋
曾敏峰
成珍
李敬荣
陈珠
郑洁
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
University of Shaoxing
Original Assignee
University of Shaoxing
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by University of Shaoxing filed Critical University of Shaoxing
Priority to CN201810485352.9A priority Critical patent/CN108786824A/zh
Publication of CN108786824A publication Critical patent/CN108786824A/zh
Pending legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/76Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
    • B01J23/83Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with rare earths or actinides
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/74General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • B01D53/86Catalytic processes
    • B01D53/8668Removing organic compounds not provided for in B01D53/8603 - B01D53/8665
    • 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
    • B01J35/391Physical properties of the active metal ingredient
    • B01J35/393Metal or metal oxide crystallite size
    • 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
    • B01J35/396Distribution of the active metal ingredient
    • 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
    • B01J35/60Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
    • B01J35/61Surface area
    • B01J35/615100-500 m2/g
    • 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
    • B01J35/60Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
    • B01J35/63Pore volume
    • B01J35/633Pore volume less than 0.5 ml/g
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2257/00Components to be removed
    • B01D2257/70Organic compounds not provided for in groups B01D2257/00 - B01D2257/602
    • B01D2257/702Hydrocarbons
    • B01D2257/7027Aromatic hydrocarbons
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2257/00Components to be removed
    • B01D2257/70Organic compounds not provided for in groups B01D2257/00 - B01D2257/602
    • B01D2257/708Volatile organic compounds V.O.C.'s

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Environmental & Geological Engineering (AREA)
  • Health & Medical Sciences (AREA)
  • Biomedical Technology (AREA)
  • Analytical Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Catalysts (AREA)

Abstract

本发明公开了一种Si柱撑粘土(SPC)负载高分散Co3O4‑CeO2催化剂的制备方法,包括两个步骤,一是SPC的制备,二是Co‑Ce/SPC的制备。本发明利用SPC为载体,通过沉积‑沉淀法合成高分散复合纳米Co3O4‑CeO2催化剂,并将其用于甲苯催化燃烧,该催化剂表现出优异的催化活性及稳定性。另外合成的SPC与蒙脱土相比,其层间距和比表面积均变大。以其为载体,制备的Co3O4‑CeO2纳米晶催化剂,活性组分颗粒小,分散均匀,催化降解甲苯的活性高,稳定性良好,是一种有良好应用前景的性能优异的降解VOC的催化材料。

Description

Si柱撑粘土负载高分散Co3O4-CeO2催化剂的制备方法及应用
技术领域
本发明涉及一种化学催化剂制备工艺技术领域,特别是一种Si柱撑粘土负载高分散Co3O4-CeO2催化剂的制备方法及应用,主要用于甲苯催化燃烧。
背景技术
Si柱撑粘土(SPC)具有大比表面积和丰富的孔结构,近年来已引起了广泛的关注。现有文献中,关于SPC多是探讨其合成方法以及对其结构和性能进行表征,或是在SPC的框架中掺杂其他物质进行改性,然后应用于以下几个方面:催化氧化脱硫、催化植物沥青裂解、异丙苯的催化裂解、催化苯氢化反应、催化苯酚羟基化反应、消除水溶液中有毒的金属离子Cr(VI)、用于可控药物释放及目标定位、催化无水叔丁基环己烯、环己烯选择性氧化等。
已有的研究中,并未发现将SPC应用于甲苯催化降解方面的报道。并且,现有的过渡金属催化剂用于甲苯催化燃烧的活性较低,因此亟需一种高活性的催化剂。
发明内容
本发明的目的是为了解决上述现有技术的不足而提供一种SPC负载高分散Co3O4-CeO2催化剂的制备方法及应用,该催化剂的活性组分分散好、同时可将其用于甲苯高效催化燃烧。
为了实现上述目的,本发明所设计的一种SPC负载高分散Co3O4-CeO2催化剂的制备方法,包括以下两个步骤:
(1)SPC的制备
将Aladdin公司的KSF无机级蒙脱土(MMT)加水,首先制备成悬浊液A,另取十二烷基二甲基苄基氯化铵阳离子表面活性剂和十二烷基硫酸钠阴离子表面活性剂溶解到乙醇中,再加入正硅酸乙酯,搅拌0.5h后得到清澈溶液B,然后将清澈溶液B慢慢滴入到悬浊液A中,搅拌0.5h,用氨水溶液调节pH至10,在25℃下搅拌2h,过滤,90℃干燥,得到样品前驱体,然后在马弗炉中空气氛围下以10℃/min的速率程序升温至550℃煅烧3h,得到稳定的SPC;
所述MMT:十二烷基二甲基苄基氯化铵阳离子表面活性剂:十二烷基硫酸钠阴离子表面活性剂:正硅酸乙酯:乙醇:水的摩尔比为1:2:0.4:30:1.2:250。
(2)Co-Ce/SPC的制备
将1.0g SPC分散在100mL去离子水中,加入1.0mol/L Co(NO3)2溶液和1.0mol/L的Ce(NO3)3·6H2O溶液,得到的混合物在25℃下充分搅拌1h,再逐滴加入1.0mol/L的氨水,调节混合物的pH至9.0,搅拌12h,离心、洗涤,70℃干燥12h,然后在马弗炉中500℃煅烧2h,得到Co-Ce/SPC催化剂,其中Co占总质量的10%,Ce占总质量的5%。
一种SPC负载高分散Co3O4-CeO2催化剂的应用在于上述Co3O4-CeO2催化剂可用于甲苯催化燃烧。
由于SPC具有大比表面积和丰富的孔结构,不仅可使大分子有机物出入这些通道或在其内孔被吸附,而且将其作为催化剂载体,可使活性组分有极高的分散度,从而提高催化燃烧甲苯的活性。本专利利用SPC为载体,通过沉积-沉淀法合成高分散复合纳米Co3O4-CeO2催化剂,并将其用于甲苯催化燃烧,该催化剂表现出优异的催化活性及耐久性。
本发明得到的一种SPC负载高分散Co3O4-CeO2催化剂的制备方法,以其为载体,制备的Co3O4-CeO2纳米晶催化剂,活性组分颗粒小,分散均匀,催化燃烧甲苯的活性高,耐久性良好,是一种有良好应用前景的性能优异的降解VOC的催化剂。
附图说明
图1是SPC负载Co-Ce催化剂用于甲苯催化燃烧的活性图;
图2是SPC负载Co-Ce催化剂的耐久性测试图;
图3是MMT和SPC的小角X射线衍射图;
图4是10%Co-5%Ce/SPC催化剂的高分辨透射电镜图。
具体实施方式
下面结合附图和实施例对本发明进一步说明。
本实施例提供的一种Si柱撑粘土负载高分散Co3O4-CeO2催化剂的制备方法,包括以下两个步骤:
(1)SPC的制备
取MMT加30mL水,首先制备成悬浊液A。另取十二烷基二甲基苄基氯化铵阳离子表面活性剂和十二烷基硫酸钠阴离子表面活性剂,溶解到乙醇中,再加入正硅酸乙酯,搅拌0.5h得到清澈溶液B。然后将清澈溶液B慢慢滴入到悬浊液A中,搅拌0.5h。用氨水溶液调节pH至10,在25℃下搅拌2h,过滤,90℃干燥,得到样品前驱体。然后在马弗炉中空气氛围下以10℃/min的速率程序升温至550℃煅烧3h,得到稳定的SPC。其中,蒙脱土:十二烷基二甲基苄基氯化铵:十二烷基硫酸钠:正硅酸乙酯:乙醇:水(摩尔比)=1:2:0.4:30:1.2:250。
(2)Co-Ce/SPC的制备
将1.0g SPC分散在100mL去离子水中,加入1.0mol/L的Co(NO3)2溶液和1.0mol/L的Ce(NO3)3·6H2O溶液。得到的混合物在25℃下充分搅拌1h。再逐滴加入1.0mol/L的氨水,调节混合物的pH至9.0,搅拌12h,离心、洗涤,70℃干燥12h。在马弗炉中500℃煅烧2h,得到10%Co-5%Ce/SPC。
下面对制得的SPC负载高分散Co3O4-CeO2催化剂进行测试,其中图1是SPC负载Co-Ce催化剂用于甲苯催化降解的活性图,活性评价实验在WFS-3010(天津,先权)反应装置上进行,空速为20000h-1,甲苯浓度为1000ppm。利用在线气相色谱(Shimadzu,GC-14C,Japan),使用氢火焰离子化检测器(FID)检测进入色谱的有机物浓度。色谱工作条件如下:汽化室温度120℃,柱温80℃。采用N2000在线色谱工作站记录分析数据。图1表明,10%Co-5%Ce/SPC在200℃使甲苯的转化率达到98.6%。
图2是SPC负载Co-Ce催化剂的耐久性测试图,耐久性实验的测试条件与活性评价实验相同。图2表明,10%Co-5%Ce/SPC在190℃下连续反应1000h,甲苯的转化率仅从96%降低到90%,具有非常良好的稳定性,而且能够有效地抵抗含氯的VOC及H2O的影响。
图3是两种载体的小角X射线衍射图,该实验在X射线粉末衍射仪(PANalytical)上进行分析,实验条件如下:CuKα射线(40mA,40kV),扫描速率为0.02°/s。利用Braggequation(2d001sinθ=nλ)计算层间距。图3表明,柱撑使蒙脱土的层间距由0.96nm增加至2.61nm。
图4是10%Co-5%Ce/SPC催化剂的高分辨透射电镜图。样品的形貌利用JEOL-2010型透射电镜表征,工作电压为200kV。图4表明,在10%Co-5%Ce/SPC中,活性组分Co3O4和CeO2的颗粒直径在5-8nm,均匀分散在SPC表面。
表1是样品的比表面积、总孔体积,具体数据如下:
aBET specific surface area.
bTotalpore volume estimated atP/P0=0.99.
样品的比表面积(SBET)、孔体积(Vp)利用TristarⅡ3020(MicromeriticsCompany,USA)全自动吸附仪表征。液氮温度(77K)下,利用N2吸附法测定SBET,利用Barrett-Joyner-Halenda(BJH)方法测定Vp
从表1中可以看出,通过Si柱撑后,MMT的SBET由30m2/g增加到453m2/g,Vp由0.11cm3/g增加到0.77cm3/g。负载Co-Ce以后,SPC的SBET和Vp均减小(453m2/g减小到303m2/g,0.77cm3/g减小到0.30cm3/g),说明部分负载组分进入了载体孔道,堵塞了一些孔。
以上所述实施例仅表达了本发明的一种实施方式,其描述较为具体和详细,但并不能因此而理解为对发明专利范围的限制。应当指出的是,对于本领域的普通技术人员来说,在不脱离本发明构思的前提下,还可以做出若干变形和改进,这些都属于本发明的保护范围。因此,本发明专利的保护范围应以所附权利要求为准。

Claims (2)

1.一种Si柱撑粘土负载高分散Co3O4-CeO2催化剂的制备方法,其特征在于,包括以下两个步骤:
(1)SPC的制备
将蒙脱土加水,首先制备成悬浊液A,另取十二烷基二甲基苄基氯化铵阳离子表面活性剂和十二烷基硫酸钠阴离子表面活性剂溶解到乙醇中,再加入正硅酸乙酯,搅拌0.5h后得到清澈溶液B,然后将清澈溶液B慢慢滴入到悬浊液A中,搅拌0.5h,用氨水溶液调节pH至10,在25℃下搅拌2h,过滤,90℃干燥,得到样品前驱体,然后在马弗炉中空气氛围下以10℃/min的速率程序升温至550℃煅烧3h,得到稳定的SPC;其中,蒙脱土:十二烷基二甲基苄基氯化铵阳离子表面活性剂:十二烷基硫酸钠阴离子表面活性剂:正硅酸乙酯:乙醇:水的摩尔比为1:2:0.4:30:1.2:250;
(2)Co-Ce/SPC的制备
将1.0g SPC分散在100mL去离子水中,加入1.0mol/L的Co(NO3)2溶液和1.0mol/L的Ce(NO3)3·6H2O溶液,得到的混合物在25℃下充分搅拌1h,再逐滴加入1.0mol/L的氨水,调节混合物的pH至9.0,搅拌12h,离心、洗涤,70℃干燥12h,然后在马弗炉中500℃煅烧2h,得到Co-Ce/SPC,其中Co占总质量的10%,Ce占总质量的5%。
2.一种如权利要求1所述的SPC负载高分散Co3O4-CeO2催化剂的应用,其特征在于:Co3O4-CeO2催化剂可用于甲苯催化燃烧。
CN201810485352.9A 2018-05-21 2018-05-21 Si柱撑粘土负载高分散Co3O4-CeO2催化剂的制备方法及应用 Pending CN108786824A (zh)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201810485352.9A CN108786824A (zh) 2018-05-21 2018-05-21 Si柱撑粘土负载高分散Co3O4-CeO2催化剂的制备方法及应用

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201810485352.9A CN108786824A (zh) 2018-05-21 2018-05-21 Si柱撑粘土负载高分散Co3O4-CeO2催化剂的制备方法及应用

Publications (1)

Publication Number Publication Date
CN108786824A true CN108786824A (zh) 2018-11-13

Family

ID=64091206

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201810485352.9A Pending CN108786824A (zh) 2018-05-21 2018-05-21 Si柱撑粘土负载高分散Co3O4-CeO2催化剂的制备方法及应用

Country Status (1)

Country Link
CN (1) CN108786824A (zh)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109772318A (zh) * 2019-01-30 2019-05-21 绍兴文理学院 LaSPC负载PtOx纳米晶催化剂的制备方法及应用

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103706353A (zh) * 2013-12-19 2014-04-09 绍兴文理学院 AlMn复合柱撑粘土负载CrCe催化剂、制备方法及其应用
CN104248948A (zh) * 2014-07-14 2014-12-31 绍兴文理学院 Ti柱撑粘土负载型催化剂、制备方法及其应用
CN105664838A (zh) * 2016-03-28 2016-06-15 中国科学院过程工程研究所 一种基于柱撑蒙脱石的脱汞吸附剂、其制备方法及用途

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103706353A (zh) * 2013-12-19 2014-04-09 绍兴文理学院 AlMn复合柱撑粘土负载CrCe催化剂、制备方法及其应用
CN104248948A (zh) * 2014-07-14 2014-12-31 绍兴文理学院 Ti柱撑粘土负载型催化剂、制备方法及其应用
CN105664838A (zh) * 2016-03-28 2016-06-15 中国科学院过程工程研究所 一种基于柱撑蒙脱石的脱汞吸附剂、其制备方法及用途

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
HUIHUI MAO ET AL.,: "Novel One-Step Synthesis Route to Ordered Mesoporous Silica-Pillared Clay Using Cationic-Anionic Mixed-Gallery Templates", 《IND. ENG. CHEM. RES.》 *
SHUFENG ZUO ET AL.,: "Promoting effect of Ce added to metal oxide supported on Al pillared clays for deep benzene oxidation", 《APPLIED CATALYSIS B: ENVIRONMENTAL》 *

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109772318A (zh) * 2019-01-30 2019-05-21 绍兴文理学院 LaSPC负载PtOx纳米晶催化剂的制备方法及应用

Similar Documents

Publication Publication Date Title
Putla et al. MnO x nanoparticle-dispersed CeO2 nanocubes: a remarkable heteronanostructured system with unusual structural characteristics and superior catalytic performance
Le et al. Ce-Mn mixed oxides supported on glass-fiber for low-temperature selective catalytic reduction of NO with NH3
Hoffmann et al. Improved catalytic methane combustion of Pd/CeO2 catalysts via porous glass integration
Soares et al. Nitrate reduction catalyzed by Pd–Cu and Pt–Cu supported on different carbon materials
Said et al. Catalytic dehydration of methanol to dimethyl ether over nanosized WO 3/Al 2 O 3 system under inert and oxidative atmosphere
Qu et al. The effects of alkali metal on structure of manganese oxide supported on SBA-15 for application in the toluene catalytic oxidation
Ying et al. Highly active and stable mesoporous Au/CeO2 catalysts prepared from MCM-48 hard-template
CN104907069A (zh) 一种用于室温甲醛净化的催化剂及其用途
Shen et al. Deactivation mechanism of potassium additives on Ti 0.8 Zr 0.2 Ce 0.2 O 2.4 for NH 3-SCR of NO
Zhang et al. MnO x–CeO 2 supported on a three-dimensional and networked SBA-15 monolith for NO x-assisted soot combustion
Varkolu et al. Hydrogenation of levulinic acid using formic acid as a hydrogen source over Ni/SiO2 catalysts
Huang et al. Carbon dioxide reforming of methane over Ni/Mo/SBA-15-La2O3 catalyst: Its characterization and catalytic performance
Nemanashi et al. Dendrimer derived titania-supported Au nanoparticles as potential catalysts in styrene oxidation
Wang et al. Insight into the Role of Pd State on Pd‐Based Catalysts in o‐Xylene Oxidation at Low Temperature
Wang et al. Low temperature combustion of VOCs with enhanced catalytic activity over MnO2 nanotubes loaded with Pt and Ni–Fe spinel
Li et al. Pt-modulated CuMnO x nanosheets as catalysts for toluene oxidation
Chai et al. Foam‐Structured NiO‐MgO‐Al2O3 Nanocomposites Derived from NiMgAl Layered Double Hydroxides In Situ Grown onto Nickel Foam: A Promising Catalyst for High‐Throughput Catalytic Oxymethane Reforming
Wu et al. Synthesis of three-dimensional ordered mesoporous MnO x/CeO 2 bimetal oxides for the catalytic combustion of chlorobenzene
Wang et al. Resin‐Derived Hierarchical Porous Carbon Spheres with High Catalytic Performance in the Oxidative Dehydrogenation of Ethylbenzene
Zhou et al. Flower-like Pt/Fe2O3–CeO2 catalysts for highly efficient low-temperature catalytic oxidation of toluene
CN110170322A (zh) 一种负载原子级贵金属的碳气凝胶催化剂的制备方法
Wang et al. Mesoporous silica-supported manganese oxides for complete oxidation of volatile organic compounds: Influence of mesostructure, redox properties, and hydrocarbon dimension
CN108786824A (zh) Si柱撑粘土负载高分散Co3O4-CeO2催化剂的制备方法及应用
Świrk et al. Investigation of Mn Promotion on HKUST‐1 Metal‐Organic Frameworks for Low‐Temperature Selective Catalytic Reduction of NO with NH3
Ren et al. Effect of activation atmosphere on the reduction behaviors, dispersion and activities of nickel catalysts for the hydrogenation of naphthalene

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
RJ01 Rejection of invention patent application after publication

Application publication date: 20181113

RJ01 Rejection of invention patent application after publication