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1.
用传统湿式浸渍法制备了La2O3掺杂的商业γ-Al2O3负载的沼气重整催化剂Ni-Co/La2O3-γ-Al2O3, 并用程序升温加氢(TPH)、程序升温氧化(TPO)、程序升温表面反应(TPSR)、程序升温脱附(TPD)及脉冲实验对催化剂进行了表征. 结果表明, 沼气重整过程中Ni-Co/La2O3-γ-Al2O3催化剂上的表面碳物种主要来源于CH4的裂解, CO2的贡献很小. CH4裂解能够产生三种活性不同的碳物种, 即Cα、Cβ与Cγ. 随着反应的进行, Cα物种减小而Cβ与Cγ物种增加, 且Cγ物种能够转变为惰性的石墨碳. 重整反应过程中CH4与CO2的活化能相互促进. 催化剂表面的O物种与C反应生成CO或与CHx反应生成CHxO再分解为CO与吸附态的H物种, 可能是Ni-Co/La2O3-γ-Al2O3催化剂上沼气重整的速率控制步骤.  相似文献   

2.
用X-射线衍射(XRD)、紫外-可见漫散射光谱(UV-Vis DRS)、程序升温还原(TPR)、CO化学吸附和微反测试等方法研究了Ni2+在γ-Al2O3上的分散状态和负载型Ni/γ-Al2O3催化剂的α-蒎烯加氢催化活性。结果表明,当Ni2+负载量远低于其在γ-Al2O3载体表面分散容量时,Ni2+优先嵌入载体表面四面体空位,随着Ni2+负载量的增加,嵌入载体表面八面体空位Ni2+的比例增大。由于八面体Ni2+易被还原为金属态Ni0,NiO/γ-Al2O3样品的还原度随Ni2+负载量的增加而大幅度地增加,经氢还原所得Ni/γ-Al2O3催化剂的CO吸附量和α-蒎烯加氢催化活性大幅度增加。对La2O3助剂的作用进行了研究,结果表明分散在γ-Al2O3上的La3+物种可阻止Ni2+嵌入γ-Al2O3表面四面体空位,增大了八面体Ni2+物种所占比例,提高了催化剂的还原度,故Ni-La2O3/γ-Al2O3催化剂催化活性高于Ni/γ-Al2O3催化剂。  相似文献   

3.
李庆远  季生福  胡金勇  蒋赛 《催化学报》2013,34(7):1462-1468
采用浸渍法制备了SiO2, γ-Al2O3, CaO和TiO2负载的Ni催化剂, 以及不同MgO含量的MgO-7.5%Ni/γ-Al2O3催化剂,利用X射线衍射和N2吸附-脱附技术表征了催化剂的结构,在固定床反应器上评价了它们在稻草水蒸气催化重整制合成气反应中的催化性能,考察了反应条件对催化剂性能的影响.结果表明, 以γ-Al2O3为载体时Ni催化剂活性最高,其中7.5%Ni/γ-Al2O3催化剂的H2收率可达1071.3ml/g,H2:CO的体积比为1.4:1;同时,MgO的添加进一步提高了该催化剂的性能,当MgO含量为1.0%时,H2收率可达1194.6ml/g,H2:CO体积比可达3.9:1.可见MgO的加入促进了Ni基催化剂上稻草水蒸气催化重整制合成气反应的进行,同时使得合成气中CO发生水-汽转换反应,从而大大提高了合成气中H2含量.  相似文献   

4.
镍基催化剂:制备及水相催化糠醛加氢脱氧反应性能   总被引:1,自引:0,他引:1  
以SiO2-Al2O3、γ-Al2O3为载体采用浸渍法制备了不同负载量的镍基催化剂,以XRD、H2-TPR、NH3-TPD与低温N2吸附等技术对催化剂特性进行了表征,并进行了水相催化糠醛加氢脱氧实验研究以制备以C5为主要成分的生物汽油。重点考察了催化剂的镍负载量、载体种类及反应温度对糠醛转化率、目标产物C5选择性的影响,并对催化剂的重复利用性能和糠醛水相加氢脱氧反应机理进行了探讨。结果表明,Ni/SiO2-Al2O3催化性能明显优于Ni/γ-Al2O3。在140 ℃、氢冷压3.0 MPa的优化反应条件下,14wt% Ni/SiO2-Al2O3催化糠醛反应的转化率为63%,C5选择性高达93%。升高反应温度可以提高糠醛的转化率,但反应产物的选择性降低。催化剂在第3次重复使用时糠醛的转化率明显降低,催化剂表面有明显的残留有机聚合物和积碳,达到25wt%左右。  相似文献   

5.
采用等体积浸渍法制备了Cu-K-La/γ-Al2O3催化剂,考察了KCl对该催化剂催化HCl氧化制Cl2反应性能的影响. 当KCl的负载量为5 wt%时,Cu-K-La/γ-Al2O3催化剂表现出较好的催化活性和稳定性,可在较大的原料气空速变化范围内使用. 在0.1 MPa,360 ℃,空速450 L/(kg-cat·h)和HCl/O2摩尔比为2:1的反应条件下,Cu-K-La/γ-Al2O3催化剂上HCl转化率在100 h内保持85%以上. 表征结果表明,Cu,K和La物种均高度分散于γ-Al2O3载体表面;一定量KCl的加入可降低Cu2+ → Cu+的还原温度,从而提高Cu2+活性中心的催化活性.  相似文献   

6.
为了提高苯乙炔加氢反应中的苯乙烯选择性, 本文采用“胶体-等体积浸渍”两步法制备了Pd-Cu/γ-Al2O3双金属催化剂. 利用高分辨率透射电镜(HRTEM)、X射线光电子能谱(XPS)、CO脉冲化学吸附、N2物理吸附、电感耦合等离子体原子发射光谱(ICP-AES)等技术表征了Pd-Cu/γ-Al2O3的结构性质, 考察了Cu/Pd 摩尔比、Pd负载量以及金属引入顺序对Pd-Cu/γ-Al2O3催化苯乙炔选择性加氢性能的影响. 结果表明, 与Pd/γ-Al2O3单金属催化剂相比, Pd-Cu/γ-Al2O3的苯乙烯选择性大幅度提高, 尤其是当Pd负载量为0.3%(w), 且Cu/Pd摩尔比为0.6时, Pd-Cu/γ-Al2O3表现出优异的加氢选择性; 在0.1 MPa和40 ℃下, 当苯乙炔转化率为90%时, 双金属催化剂的苯乙烯选择性可达95%; 当转化率达到99%以上时, 苯乙烯选择性仍保持在82%左右. 分析表明, Pd-Cu/γ-Al2O3中形成了Pd-Cu合金, 但是两种金属间不存在电子转移, Cu对Pd的几何效应才是导致Pd-Cu/γ-Al2O3苯乙烯选择性增加的主要原因.  相似文献   

7.
 研究了 Mo 和 Cu 助剂对 FeK/SiO2 催化剂的性质及费托 (F-T) 合成性能的影响. 采用 N2 物理吸附、H2 程序升温还原、X 射线衍射、穆斯堡尔谱和 X 射线光电子能谱技术对催化剂进行了表征. 结果表明, Mo 加入后与 Fe 产生了较强的相互作用, 抑制了催化剂的还原和碳化; Cu 助剂的加入促进了催化剂的还原和碳化; 当 Mo 和 Cu 共同加入后, 催化剂的还原和碳化行为与单独加入 Cu 助剂时相似. 催化剂 F-T 合成性能在固定床上于 280 oC, 1.5 MPa, 2 000 h-1, H2/CO = 2.0 的合成气中测试. 结果表明, Mo 的加入降低了催化剂活性, 但提高了重质烃 (C5+) 的选择性; Cu 的添加提高了催化剂的活性, 但对稳定 C5+选择性作用不明显. Mo 和 Cu 共同加入后, 催化剂既表现出较为稳定的 C5+选择性, 同时其活性也没有降低.  相似文献   

8.
采用分步浸渍法制备负载型Ru-Fe3O4/γ-Al2O3 催化剂, 并利用透射电子显微镜(TEM)、X 射线衍射(XRD)、N2吸附-脱附(BET)、傅里叶变换红外(FTIR)光谱与X射线光电子能谱(XPS)表征催化剂的纳米颗粒粒径分布、晶相组成、表面结构及吸附物种等性质. 将Ru-Fe3O4/γ-Al2O3催化剂用于3,4-二氯硝基苯选择性原位液相加氢反应, 考察了反应条件对催化活性的影响, 并讨论了不同制备条件下催化剂的稳定性能. 结果表明, 在473 K、液压3 MPa、原料质量分数2%, 乙醇/水体积比75:25 的反应条件下, 3,4-二氯硝基苯的转化率为100%, 3,4-二氯苯胺的选择性高达96.4%. Fe3O4含量对催化剂稳定性能有显著影响, 当Ru和Fe 的质量分数分别为2%和6%时, 催化剂可稳定200 h以上. 表面吸附CO与积碳是导致催化剂失活的主要原因, 以Fe3O4作为高效的助剂, 进行水汽转换(WGS)反应与费托合成(FTS)可移除CO, 而采用煅烧法去除表面积碳. 晶相变化与纳米颗粒的聚集可能导致催化剂部分失活, 其原因以及再生方法需进一步考察.  相似文献   

9.
尉继英  范桂芳  江锋  张振中  张兰 《催化学报》2010,31(12):1489-1495
 采用沉积沉淀法制备了 CO 低温氧化催化剂 Au/α-Fe2O3, 通过 X 射线衍射、X 射线光电子能谱、N2 吸附-脱附、傅里叶变换红外光谱、H2 程序升温还原和 CO2 程序升温脱附等手段对催化剂进行了表征, 探讨了在室温大气气氛下光线照射以及表面吸附等环境因素所导致的催化剂存贮失活及其作用机理. 结果表明, 经 110 oC 干燥的 Au/α-Fe2O3催化剂表面同时存在 Au3+和 Auδ+ (0 ≤ δ ≤ 1) 物种, 且前者催化 CO 氧化的活性更高; 在室温大气气氛下, 紫外线照射会引起 Au3+的还原和 Au 颗粒的生长, 导致催化剂的不可逆失活. 此外, 空气中的 H2O 和 CO2 可同时吸附在 α-Fe2O3的表面, 形成表面碳酸盐物种, 会引起催化剂的可逆失活.  相似文献   

10.
H2SO4处理的Nb2O5/γ -Al2O3催化剂表面酸性与催化性能研究   总被引:3,自引:0,他引:3  
用Hammett指示剂法、红外光谱(IR)、示差扫描量热-热重法(DSC-TG)和微型催化反应装置等研究了H2SO4处理的负载型Nb2O5/γ-Al2O3催化剂表面酸性和催化异丁烯(IB)与异丁醛(IBA)反应生成2,5-二甲基-2,4-己二烯(DMHD)的催化性能。结果表明随所用H2SO4浓度增加,Nb2O5/γ-Al2O3催化剂表面酸性增强,B酸量增加,L酸量先增加后下降。经H2SO4处理的Nb2O5/γ-Al2O3催化剂的催化活性明显增加,但当H2SO4浓度超过0.05 mol·L-1时催化活性又急剧下降,这可能是因为在H2SO4处理的催化剂表面形成的强酸中心上,产物分子进一步转化为积炭且封闭催化剂活性表面,导致催化活性下降。  相似文献   

11.
16.6%Co/γ-Al_2O_3 catalysts prepared by incipient wetness impregnation method were used for Fischer-Tropsch synthesis.The support was pre-treated with different concentration of NH_4NO_3 aqueous solution.The effect of support pre-treatment on the properties of support and performance of supported- cobalt-based catalysts was investigated.To treat the support with NH_4NO_3 aqueous solution enlarged the pore ofγ-Al_2O_3,decreased the impurity Na_2O content,and weakened the surface acidity ofγ-Al_2O_3. The change in the properties of the support decreased the interaction between cobalt species and support, enhanced the CO hydrogenation rate and the C_(5 )selectivity.For all catalysts,increasing the reaction temperature increased the CO hydrogenation rate or the CO conversion,slightly decreased the total hydrocarbon selectivity,and favored the formation of methane and light hydrocarbons,while the chain growth probability decreased.For 16.6%Co/γ-Al_2O3 catalysts,prepared with the support treated with 100 g/L NH_4NO3 aqueous solution,the CO conversion,the CH_4 selectivity,and the C_(5 )selectivity were 83.13%,6.86% and 82.75% respectively,and the chain growth probability was 0.83 under the condition of 493 K,1.5 MPa,500 h~(-1)and the molar ratio of H_2 to CO being 2.0 in feed.  相似文献   

12.
采用浸渍法制备了Co-Pt-ZrO2/γ-Al2O3催化剂,对其进行了BET、XRD和TPR等表征,并在浆态床反应器上考察了焙烧温度和还原温度对催化剂费托合成反应性能的影响。结果表明,焙烧温度过高,容易造成Co物种和载体间的相互作用增强,使部分氧化钴颗粒聚集或烧结,导致催化剂的F-T合成反应活性和C5+烃选择性降低。还原温度较低时,钴物种不能充分还原,CO加氢活性低,甲烷选择性高,重质烃选择性低;还原温度过高,则可能造成活性物种的烧结,反而降低了催化剂的活性和重质烃选择性。在原料气n(H2)/n(CO)=2.0、483 K、2.4 MPa和空速3.6 L/(gcat·h)的条件下,31.08%Co~0.11%Pt~7.16%ZrO2/Al2O3催化剂在673 K焙烧。纯H2下653 K还原后,其费托性能最佳;CO转化率为27.0%,C5+的选择性为83.0%。  相似文献   

13.
NO reduction by CO was investigated over CuO/γ-Al2O3, Mn2O3/γ-Al2O3, and CuOMn2O3/γ-Al2O3 model catalysts before and after CO pretreatment at 300 °C. The CO-pretreated CuO-Mn2O3/γ-Al2O3 catalyst exhibited higher catalytic activity than did the other catalysts. Based on X-ray diffraction (XRD), X-ray photoelectron spectroscopy (XPS), UV/Vis diffuse reflectance spectroscopy (DRS), Raman, and H2-temperature-programmed reduction (TPR) results, as well as our previous studies, the possible interaction model between dispersed copper and manganese oxide species as well as γ-Al2O3 surface has been proposed. In this model, Cu and Mn ions occupied the octahedral vacant sites of γ-Al2O3, with the capping oxygen on top of the metal ions to keep the charge conservation. For the fresh CuO/γ-Al2O3 and Mn2O3/γ-Al2O3 catalysts, the -Cu-O-Cu- and -Mn-O-Mn- species were formed on the surface of γ-Al2O3, respectively; but for the fresh CuO-Mn2O3/γ-Al2O3 catalyst, -Cu-O-Mn- species existed on the surface of -Al2O3. After CO pretreatment, -Cu-□-Cu- and -Mn-□-Mn- (□ represents surface oxygen vacancy (SOV)) species would be formed in CO-pretreated CuO/γ-Al2O3 and CO-pretreated Mn2O3/γ-Al2O3 catalysts, respectively; whereas -Cu-□-Mn- species existed in CO-pretreated CuO-Mn2O3/γ-Al2O3. Herein, a new concept, surface synergetic oxygen vacancy (SSOV), which describes the oxygen vacancy formed between the individual Mn and Cu ions, is proposed for CO-pretreated CuO-Mn2O3/γ-Al2O3 catalyst. In addition, the role of SSOV has also been approached by NO temperature-programmed desorption (TPD) and in situ FTIR experiments. The FTIR results of competitive adsorption between NO and CO on all the CO-pretreated CuO/γ-Al2O3, Mn2O3/γ-Al2O3, and CuO-Mn2O3/γ-Al2O3 samples demonstrated that NO molecules mainly were adsorbed on Mn2+ and CO mainly on Cu+ sites. The current study suggests that the properties of the SSOVs in CO-pretreated CuO-Mn2O3/γ-Al2O3 catalyst were significantly different to SOVs formed in CO-pretreated CuO/γ-Al2O3 and Mn2O3/γ-Al2O3 catalysts, and the SSOVs played an important role in NO reduction by CO.  相似文献   

14.
设计并制备了Ni-V/γ-Al2O3催化剂, 研究了其上苯用过氧化氢氧化氨化一步直接合成苯胺的性能和不同氨基源对合成苯胺的影响. 实验结果显示:在本文条件下, Ni/γ-Al2O3和V/γ-Al2O3催化剂均能活化苯环上C—H键, 使苯一步氧化羟基化为苯酚. Ni、V双组分催化剂则表现出较好的合成苯胺活性和选择性, 催化剂中Ni/V摩尔比在5.5时催化活性和选择性最好,目标产物苯胺的选择性达到85%, 远远高于主要副产物苯酚的选择性. 反应时间宜控制在2 h左右, 反应最佳温度为333 K. 尿素在碱性条件下可作为氨基化试剂, 在Ni-V/γ-Al2O3催化剂作用下使苯直接氧化氨化为苯胺, 尿素和氨水作为共氨化剂表现出对生成苯胺有利的协同效应.  相似文献   

15.
采用并流淤浆混合法制备了一系列具有不同铜锌铝比的铜基甲醇合成催化剂CuO/ZnO/Al2O3,测试了其催化性能(甲醇收率和CO转化率)及物相结构,并对该制备方法进行评价。Cu∶Zn∶Al摩尔比为4∶5∶1 的铜基催化剂显示了最好的催化活性。通过对催化剂前驱物煅烧过程进行DTA分析及对前驱物进行XRD分析表明, 催化剂前驱物的物相与Al2O3的量有关。当Al2O3的量较低时,前驱物的物相以(Cu0.3 Zn0.7)5(CO3)2(OH)6为主;当Al2O3的量较高时,前驱物中物相(Cu0.3Zn0.7)5(CO3)2(OH)6的量下降,而物相Cu2CO3(OH)2的量增加。物相(Cu0.3 Zn0.7)5(CO3)2(OH)6对终态催化剂的活性是十分有利的 。  相似文献   

16.
The effect of vanadium addition to Cu/γ-Al2O3 catalyst used in the hydrogenation of CO2 to produce methanol was studied. It was found that the catalytic performance of the Cu-based catalyst improved after V addition. The influence of reaction temperature, space velocity and the molar ratio of H2 to CO2 on the performance of 12%Cu-6%V/γ-Al2Oa catalyst were also studied. The results indicated that the best conditions for reaction were as follows: 240 ℃, 3600 h-1 and a molar ratio of H2 to CO2 the dispersion of the supported CuO species, which resulted in the enhanced catalytic performance of Cu-V/γ-Al2O3 binary catalyst.  相似文献   

17.
K改性β-Mo2C催化剂CO加氢合成低碳混合醇的研究   总被引:3,自引:3,他引:0  
制备系列K改性的β-Mo2C催化剂并对其CO加氢合成低碳混合醇性能进行了考察。结果表明,K改性使β-Mo2C催化剂的CO加氢选择性发生显著变化。β-Mo2C催化剂CO加氢的产物主要为C1~C4烷烃,经K改性后β-Mo2C催化剂上产物主要为C1~C5低碳醇,其中高级醇(C2+OH)选择性可达到33.78%。通过对碱金属质量分数的考察发现,当K/Mo(原子比)为0.2时,总醇选择性达到最大值,低碳醇的时空收率达到0.12 g/(mL·h-1)。β-Mo2C催化剂上醇烃产物均符合线性Anderson-Schultz-Flory(A-S-F)分布曲线,而K改性β-Mo2C催化剂上醇产物为独特的甲醇负偏离A-S-F分布。可见,K助剂的加入有效促进了低碳醇的形成,尤其是促进了C1OH到C2OH的链增长步骤。  相似文献   

18.
A series of Cu/Zn based catalysts with and without Ni, prepared by the co-precipitation method, has been studied for methanol decomposition. CO and H2 are the major products. The Cu/Zn catalysts show a low initial activity and a poor stability. The formation of the CuZn alloys was observed in the deactivated Cu/Zn catalysts which were used for methanol decomposition at 250 . When small amounts of Ni were added in the catalyst, the Cu/Zn/Ni(molar ratio 5/4/ x) catalysts showed a high activity at a low temperature. The activity and the stability of the catalyst depend on the nickel content. The activity of the Cu/Zn/Ni catalysts was maintained at a. relatively stable value of 78% conversion of methanol with 95% selectivity of H2, 93% selectivity of CO, and a more than 70% yield of hydrogen was obtained at 250 C when x >1. The stability of the Cu/Zn/Ni (molar ratio 5/4/x) catalysts showed the maximum (ca 88%) when x=1. The stabilization effect of nickel on the Cu/Zn based catalysts may lead to the increasin  相似文献   

19.
采用色谱-微反流动法反应装置考察了w%CuO/15%TiO2/γ-Al2O3催化剂对NO+CO的反应活性;催化剂经空气氛或氢气氛预处理后,NO转化率达100%的反应温度分别是325和275 ℃;XRD仅能检测到γ-Al2O3晶相,负载15%CuO后可以检测到微弱的CuO晶相;H2-TPR能检测到2个CuO的还原峰(α和β峰),将其归属于高度分散的CuO分别在裸露的γ-Al2O3和TiO2/γ-Al2O3载体上的还原;原位红外分析结果表明催化剂经空气氛或氢气氛预处理后,吸附NO+CO反应气后,反应的中间产物N2O出现的温度分别为200和150 ℃。  相似文献   

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