CN111659404B - 一种负载型核壳结构ZnO催化剂及其制备方法和应用 - Google Patents
一种负载型核壳结构ZnO催化剂及其制备方法和应用 Download PDFInfo
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- 238000006356 dehydrogenation reaction Methods 0.000 claims abstract description 27
- 229910003962 NiZn Inorganic materials 0.000 claims abstract description 26
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Abstract
本发明属于负载型催化剂技术领域,公开了一种负载型核壳结构ZnO催化剂及其制备方法和应用,该催化剂以Al2O3为载体,以ZnO为活性位;Al2O3载体负载有NiZn@ZnO核壳结构,NiZn@ZnO核壳结构包括NiZn合金内核和ZnO外壳;制备方法为先将Ni(NO3)3·6H2O和Zn(NO3)2·6H2O溶于去离子水中;然后将Al2O3浸渍于上述所得溶液中,超声分散均匀后完全干燥;最后所得固体焙烧,还原后得到目标催化剂。本发明的催化剂具有高活性和高选择性,并表现出优异的稳定性,打破了ZnO基催化剂快速失活的限制,可以在低碳烷烃脱氢制烯烃,特别是丙烷脱氢制丙烯中应用。
Description
技术领域
本发明属于负载型催化剂技术领域,具体来说,是涉及一种Al2O3负载的NiZn@ZnO核壳结构催化剂及其制备方法和应用。
背景技术
丙烯是工业生产重要的基础化工原料之一,主要用于生产聚丙烯、环氧丙烷、丙烯腈等产品。近年来,全球范围内丙烯的需求量大增,促进了其产能快速增长,国内2019年丙烯总产量达到3300万吨,同比2018年涨幅在8.75%。目前,丙烯供应主要来自石脑油裂解制乙烯和石油催化裂化过程的副产品。但是,随着富含低碳烷烃的页岩气的开发,乙烯生产工艺开始从石脑油裂解转向乙烷蒸汽裂解等非联产丙烯技术,因而丙烯价格也随之上升。加上传统工艺的高耗能、低选择性以及石油资源的短缺,无法满足日益增长的需求,促使人们寻找更经济更高效的丙烯生产方式。而丙烯-丙烷价差自2016年来持续扩大,丙烷脱氢借助成本优势产能增加显著,丙烷脱氢制丙烯技术(PDH)展现出了广阔的前景。2013年10月,天津渤化年产能60万吨的丙烷脱氢装置的投产,丙烷脱氢大幕在中国正式拉开。2014-2016年间,丙烷脱氢(含混烷)产能已每年至少投产三套装置的速度增长。截止2017年底,中国丙烷脱氢(含混烷)总产能达513.5万吨,在总产能中占比达15%。
丙烷脱氢的反应式为:△H298K=124.3kJ/g.mol。反应是受热力学平衡控制的强吸热反应,高温、低压条件有利于反应的进行。负载型CrOx和Pt催化剂是两类重要的工业催化剂,分别应用于丙烷脱氢已经工业化的生产工艺;即Lummus的Catofin工艺和UOP的Oleflex工艺中,Catofin工艺采用的CrOx催化剂受积碳失活困扰,平均12分钟就要对催化剂再生一次,同时CrOx也会对环境造成严重污染。而Oleflex工艺选用的Pt系催化剂具有优异的活化烷烃C-H键的能力,但作为贵金属,Pt的应用受到其昂贵价格的强烈限制。因此,廉价且环境友好的替代催化剂受到广泛关注。
在具有催化丙烷脱氢活性的各种金属氧化物中(氧化钒,氧化镓,氧化铁,氧化锆等),氧化锌具有较高的活性和对丙烯的选择性,储量丰富且廉价易得,是很有潜力的催化剂。目前存在的问题是氧化锌作为活性物种,在丙烷脱氢反应过程中暴露于还原性的反应气氛下容易快速失活,失活的机制是脱氢反应过程中ZnO活性位点上表面羟基和烷基锌的H重组时H2O的形成和脱附导致的ZnO物种还原金属Zn,金属Zn无丙烷脱氢活性且熔点较低易流失。
发明内容
本发明要解决的是现有ZnO基催化剂容易快速失活的技术问题,提供了一种负载型核壳结构ZnO催化剂及其制备方法和应用,该催化剂具有高活性和高选择性,廉价无毒,与此同时表现出优异的稳定性,打破了ZnO基催化剂快速失活的限制,可以在低碳烷烃脱氢制烯烃中作为催化剂应用。
为了解决上述技术问题,本发明通过以下的技术方案予以实现:
根据本发明的一个方面,提供了一种负载型核壳结构ZnO催化剂,该催化剂以Al2O3为载体,以ZnO为活性位;Al2O3载体负载有NiZn@ZnO核壳结构,NiZn@ZnO核壳结构包括NiZn合金内核和ZnO外壳;该催化剂分子式记为NixZny/Al2O3,x:y=(1:1)-(1:4)。
进一步地,以催化剂中Al2O3载体质量为基准,Ni的质量百分含量为1%-3%。
更进一步地,以催化剂中Al2O3载体质量为基准,Ni的质量百分含量为0.5%-6%。
进一步地,x:y=1:3。
根据本发明的另一个方面,提供了一种所述负载型核壳结构ZnO催化剂的制备方法,该方法按照以下步骤进行:
(1)将Ni(NO3)3·6H2O和Zn(NO3)2·6H2O溶于去离子水中;
(2)将Al2O3浸渍于步骤(1)所得溶液中,超声分散均匀后完全干燥;
(3)将步骤(2)所得固体在500-600℃焙烧2-4h,还原后得到Al2O3负载的NiZn@ZnO核壳结构催化剂。
进一步地,步骤(2)中的干燥过程为在室温下自然干燥后,在80-100℃下完全干燥。
进一步地,步骤(3)中的还原温度为500-700℃,还原时间为1-2h。
根据本发明的另一个方面,提供了一种所述负载型核壳结构ZnO催化剂在低碳烷烃脱氢制烯烃中的应用。
进一步地,所述低碳烷烃为丙烷,所述烯烃为丙烯。
本发明的有益效果是:
本发明的负载型核壳结构ZnO催化剂,以廉价易得的非贵金属氧化物ZnO为活性组分,与工业上常用的贵金属Pt系催化剂相比大大降低了催化剂的成本,利用强相互作用(SMSI)构建了内核是NiZn合金,外壳是ZnO的NiZn@ZnO核壳结构,这种NiZn合金与ZnO之间强烈的相互作用以及伴随的NiZn合金与ZnO之间的电子转移可以显著改变ZnO的几何结构和电子性质,从而改变脱氢反应过程中ZnO活性中心O位点对H的结合强度,抑制H2O的形成和脱附从而抑制ZnO的还原失活,与已有报道的其他ZnO基脱氢催化剂相比稳定性显著提升。通过多种表征手段证实ZnO壳层的完全包覆,催化剂表面没有Ni位点的暴露,避免具有C-H断键活性和高C-C断键活性的Ni位点对脱氢选择性造成不利影响,保持ZnO基脱氢催化剂的高选择性。
本发明的催化剂采用共浸渍法制备,原料易得,过程简单,重复性高,具有一定的工业意义。
本发明的催化剂对低碳烷烃脱氢制烯烃具有良好的催化效果,在高温条件下低碳烷烃转化率可达40%以上,烯烃选择性可达到90%以上,与此同时表现出优异的稳定性,打破了ZnO基催化剂快速失活的限制。
附图说明
图1为实施例1-6所制得催化剂的催化性能图;其中,(a)为丙烷转化率随时间变化曲线,(b)为丙烯选择性随时间变化曲线,(c)为失活速率常数kd计算结果图。
图2为实施例1、7、8、9所制备催化剂的催化性能图。
图3为实施例1、14、15所制得的Ni1Zn3/Al2O3催化剂的催化性能图。
图4为实施例1所制得的Ni1Zn3/Al2O3催化剂的550℃再生稳定性测试图。
图5为实施例1、2、4、5所制得催化剂的XRD谱图,其中I、II、III、IV分别对应实施例5、4、2、1。
图6为实施例1所制得Ni1Zn3/Al2O3催化剂的EDS-mapping图。
图7为实施例1所制得Ni1Zn3/Al2O3催化剂的TEM图。
图8为实施例1、5、6所制得催化剂随He气吹扫时间变化CO吸附红外结果对比图;其中,(a)、(b)、(c)分别对应实施例5、实施例1、实施例6所制得催化剂。
图9为实施例1、2、4、5所制得催化剂的催化活性与Ni金属表面积关系图;其中,(a)为实施例1、2、4、5所制得催化剂的Ni金属表面积测量结果图;(b)为丙烷转化率随Ni金属表面积变化关系图。
图10为实施例1、6所制得催化剂H2-TPD测试结果图;其中,(a)、(b)分别对应实施例6、实施例1所制得催化剂。
具体实施方式
下面通过具体的实施例对本发明作进一步的详细描述,以下实施例可以使本专业技术人员更全面的理解本发明,但不以任何方式限制本发明。
实施例1
(1)将0.15质量份的Ni(NO3)3·6H2O和0.45质量份的Zn(NO3)2·6H2O溶于1mL的去离子水中;
(2)将1质量份Al2O3浸渍于上述溶液,超声0.5h-1h,在室温下自然干燥12h,然后在80-100℃下完全干燥;
(3)将(2)得到的固体在600℃空气气氛下焙烧3h,在600℃下还原1h,得到Al2O3负载的NiZn@ZnO核壳结构催化剂,该催化剂以其中载体质量为基准,Ni的质量百分含量为3%,分子式记为Ni1Zn3/Al2O3;
(4)将制备好的Al2O3负载的NiZn@ZnO核壳结构催化剂压片为20-40目的颗粒状催化剂;
(5)将压片后的Al2O3负载的NiZn@ZnO核壳结构颗粒状催化剂装入固定床反应器,通入反应气进行反应,反应气中氢气和丙烷的摩尔比为1:1,丙烷质量空速为4h-1,平衡气为氮气。
实施例2:
用实施例1方法进行制备和反应,其区别仅在于步骤(1)中取0.15质量份的硝酸锌(Zn(NO3)2·6H2O);所得催化剂以载体质量为基准,Ni的质量百分含量为3%,分子式记为Ni1Zn1/Al2O3。
实施例3:
用实施例1方法进行制备和反应,其区别仅在于步骤(1)中取0.6质量份的硝酸锌(Zn(NO3)2·6H2O);所得催化剂以载体质量为基准,Ni的质量百分含量为3%,分子式记为Ni1Zn4/Al2O3。
实施例4:
用实施例1方法进行制备和反应,其区别仅在于步骤(1)中取0.05质量份的硝酸锌(Zn(NO3)2·6H2O);所得催化剂以载体质量为基准,Ni的质量百分含量为3%,分子式记为Ni3Zn1/Al2O3。
实施例5:
用实施例1方法进行制备和反应,其区别仅在于步骤(1)中取0质量份的硝酸锌(Zn(NO3)2·6H2O);所得催化剂以载体质量为基准,Ni的质量百分含量为3%,分子式记为Ni/Al2O3。
实施例6:
用实施例1方法进行制备和反应,其区别仅在于步骤(1)中取0质量份的硝酸镍Ni(NO3)3·6H2O,所得催化剂以载体质量为基准,Zn的质量百分含量为10%,分子式记为ZnO/Al2O3。
实施例7:
用实施例1方法进行制备和反应,其区别仅在于步骤(1)中取0.025质量份的硝酸镍Ni(NO3)3·6H2O,所得催化剂以载体质量为基准,Ni的质量百分含量为0.5%,分子式记为Ni1Zn3/Al2O3。
实施例8:
用实施例1方法进行制备和反应,其区别仅在于步骤(1)中取0.05质量份的硝酸镍Ni(NO3)3·6H2O,所得催化剂以载体质量为基准,Ni的质量百分含量为1%,分子式记为Ni1Zn3/Al2O33。
实施例9:
用实施例1方法进行制备和反应,其区别仅在于步骤(1)中取0.3质量份的硝酸镍Ni(NO3)3·6H2O,所得催化剂以载体质量为基准,Ni的质量百分含量为6%,分子式记为Ni1Zn3/Al2O3。
实施例10:
用实施例1方法进行制备和反应,其区别仅在于步骤(3)中的焙烧温度为400℃。
实施例11:
用实施例1方法进行制备和反应,其区别仅在于步骤(3)中的焙烧温度为500℃。
实施例12:
用实施例1方法进行制备和反应,其区别仅在于步骤(3)中的焙烧时间为2h。
实施例13:
用实施例1方法进行制备和反应,其区别仅在于步骤(3)中的焙烧时间为4h。
实施例14:
用实施例1方法进行制备和反应,其区别仅在于步骤(3)中的还原温度为500℃。
实施例15:
用实施例1方法进行制备和反应,其区别仅在于步骤(3)中的还原温度为700℃。
实施例16:
用实施例1方法进行制备和反应,其区别仅在于步骤(3)中的还原时间为2h。
对于上述实施例所制备的催化剂进行丙烷脱氢反应催化性能的测试,催化剂活性以丙烷转化率和丙烯选择性及失活速率表示,结合计算结果讨论如下:
对实施例1-6对应不同Ni/Zn比的催化剂进行丙烷脱氢反应催化性能的测试,催化性能如图1所示,其中(a)为丙烷转化率随时间变化曲线,(b)为丙烯选择性随时间变化曲线,(c)为失活速率常数kd计算结果图。从图1中可以看出,实施例1-3对应的NixZny/Al2O3催化剂稳定性有了显著提升;而实施例5的纯Ni/Al2O3表现出高的初始活性,但对丙烯的选择性差,并且经历了由于快速的焦炭沉积覆盖了高活性位点而快速失活的诱导期,然后变为相对稳定和低活。实施例6的ZnO/Al2O3对丙烯选择性可达90%以上,但具有连续快速失活的倾向,失活速率常数(kd)高于0.37h-1,表明丙烷脱氢反应过程中稳定性较差。另外,从图1中可以看出,随着Zn添加量的增加,NixZny/Al2O3的催化行为趋于从类Ni转变为类ZnO,这可能暗示了活性位的转变。与ZnO相比,Ni1Zn3/Al2O3失活趋势得到显著抑制,并且具有更高的活性和相似的选择性,初始所得丙烷转化率为37%,选择性可达90%以上。
实施例1、7、8、9为不同Ni质量百分含量(以载体质量为基准)所制得催化剂及其进行的丙烷脱氢制烯烃反应,催化性能如图2所示,可以看到随Ni含量的增加丙烷转化率逐渐增加,但当Ni含量增加到6wt%时,丙烯选择性大幅下降,可能是更高的Ni含量导致部分Ni位点的暴露。当Ni质量百分含量为3wt%时催化性能最优。
实施例1、14、15为在不同还原温度条件下所制得催化剂及其进行的丙烷脱氢制烯烃反应,催化性能如图3所示,可以看到还原温度在500℃到600℃区间催化性能没有发生显著变化,但当还原温度提高至700℃时,催化剂丙烷转化率显著降低,这是由于700℃的还原温度会导致作为活性物种的ZnO深度还原,形成熔点较低(420℃)且无活性的金属态Zn,导致活性的损失。
进一步对实施例1所制得催化剂在550℃下进行了长时间再生稳定性测试,结果如图4所示,在保持稳定的90%以上选择性的同时,Ni1Zn3/Al2O3催化剂失活速率常数(kd)低至0.017h-1,表现出优异的长时间稳定性,打破了ZnO基催化剂快速失活的限制。
对实施例1、2、4、5对应不同Ni/Zn比的催化剂进行XRD分析,结果如图5所示,其中I、II、III、IV分别对应实施例5、4、2、1,可以看到随Zn含量的增加Zn逐渐渗透到Ni的体相晶格中,衍射峰由Ni(111)向NiZn(101)发生转变,形成了体相NiZn合金。
对实施例1所制得Ni1Zn3/Al2O3催化剂进行EDS-mapping分析,结果如图6所示,得到均一的Ni和Zn元素分布并无分相发生,表明Ni1Zn3形成体相NiZn合金同时可能存在Zn的表面偏析。
结合图7所示,对实施例1所制得Ni1Zn3/Al2O3催化剂用高倍TEM分析通过对晶格条纹的识别发现,Ni1Zn3体相NiZn合金的表面存在着均匀的ZnO包覆层,形成了内核是NiZn合金,外壳是ZnO的核壳结构。
对实施例1、5、6所制得催化剂进行表面敏感的CO吸附红外实验,结果如图8所示,其中(a)、(b)、(c)分别对应实施例5、实施例1、实施例6所制得催化剂,发现Ni1Zn3对比纯Ni看不到2055cm-1处Ni的CO吸附峰,同时2198cm-1处出现了ZnO的CO线式吸附峰,1696和1522cm-1处出现ZnO表面一些碳酸盐物种的吸附峰,证实了由强相互作用诱导的ZnO反向包覆Ni现象的发生。
进一步实施例1、2、4、5所制得催化剂通过氢脉冲吸附测量了Ni的活性表面积,如图9所示,其中(a)为Ni金属表面积测量结果图;(b)为丙烷转化率随Ni金属表面积变化关系图。可以看到随Zn含量的增加,Ni的活性表面积先升高随后一直下降,一开始的升高可能是因为初始NiZn合金的形成改善了Ni的表面分散,而Zn的继续添加则会在合金表面形成ZnO包覆层,导致Ni活性表面积的下降,最重要的是,对于Ni1Zn3得到了一个接近于零的Ni活性表面积数值,证实了ZnO对Ni的完全包覆,表面没有Ni的暴露,而与此同时丙烷的动力学区间转化率却达到了最高,可以排除合金位或者界面位的Ni是活性位点的假设,证实了核壳结构中壳层ZnO是丙烷脱氢的活性位点。
对实施例1、6所制得催化剂进行H2-TPD实验,结果如图10所示,其中,(a)、(b)分别对应实施例6、实施例1所制得催化剂。H2-TPD实验结果可以解释NiZn@ZnO对ZnO物种失活的抑制效果,由于强相互作用诱导的核壳结构改变了Zn和O位点的几何环境以及壳层ZnO向内核合金的ZnO转移电子降低了O位点上的电子密度,减弱了对氢的结合能力,导致O-H键解离比Zn-OH键解离更容易,促进了H2的形成和脱附而不是H2O,从而抑制了ZnO的还原失活,导致稳定性的提高。
尽管上面结合附图对本发明的优选实施例进行了描述,但是本发明并不局限于上述的具体实施方式,上述的具体实施方式仅仅是示意性的,并不是限制性的,本领域的普通技术人员在本发明的启示下,在不脱离本发明宗旨和权利要求所保护的范围情况下,还可以作出很多形式的具体变换,这些均属于本发明的保护范围之内。
Claims (9)
1.一种负载型核壳结构ZnO催化剂,其特征在于,该催化剂以Al2O3为载体,以ZnO为活性位;Al2O3载体负载有NiZn@ZnO核壳结构,NiZn@ZnO核壳结构包括NiZn合金内核和ZnO外壳;该催化剂分子式记为NixZny/Al2O3,x:y=(1:1)- (1:4)。
2.根据权利要求1所述的一种负载型核壳结构ZnO催化剂,其特征在于,以催化剂中Al2O3载体质量为基准,Ni的质量百分含量为1%-3%。
3.根据权利要求1所述的一种负载型核壳结构ZnO催化剂,其特征在于,以催化剂中Al2O3载体质量为基准,Ni的质量百分含量为0.5%-6%。
4.根据权利要求1所述的一种负载型核壳结构ZnO催化剂,其特征在于,x:y=1:3。
5.一种如权利要求1-4中任一项所述负载型核壳结构ZnO催化剂的制备方法,其特征在于,该方法按照以下步骤进行:
(1)将Ni(NO3)3·6H2O 和Zn(NO3)2·6H2O溶于去离子水中;
(2)将Al2O3浸渍于步骤(1)所得溶液中,超声分散均匀后完全干燥;
(3)将步骤(2)所得固体在500-600℃焙烧2-4 h,还原后得到Al2O3负载的NiZn@ZnO核壳结构催化剂。
6.根据权利要求5所述的一种负载型核壳结构ZnO催化剂的制备方法,其特征在于,步骤(2)中的干燥过程为在室温下自然干燥后,在80-100℃下完全干燥。
7.根据权利要求5所述的一种负载型核壳结构ZnO催化剂的制备方法,其特征在于,步骤(3)中的还原温度为500-700℃,还原时间为1-2h。
8.一种如权利要求1-4中任一项所述负载型核壳结构ZnO催化剂在低碳烷烃脱氢制烯烃中的应用。
9.根据权利要求8所述的一种所述负载型核壳结构ZnO催化剂在低碳烷烃脱氢制烯烃中的应用,其特征在于,所述低碳烷烃为丙烷,所述烯烃为丙烯。
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