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Improvement strategies for Ni-based alcohol steam reforming catalysts 被引量:1
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作者 Alex Desgagnés Ommolbanin Alizadeh Sahraei Maria C.Iliuta 《Journal of Energy Chemistry》 SCIE EI CAS CSCD 2023年第11期447-479,I0010,共34页
Steam reforming(SR)of fossil methane is already a well-known,documented and established expertise in the industrial sector as it accounts for the vast majority of global hydrogen production.From a sustainable developm... Steam reforming(SR)of fossil methane is already a well-known,documented and established expertise in the industrial sector as it accounts for the vast majority of global hydrogen production.From a sustainable development perspective,hydrogen production by SR of biomass-derived feedstock represents a promising alternative that could help to lower the carbon footprint of the traditional process.In this regard,bio-alcohols such as methanol,ethanol or glycerol are among the attractive candidates that could serve as green hydrogen carriers as they decompose at relatively low temperatures in the presence of water compared to methane,allowing for improved H_(2)yields.However,significant challenges remain regarding the activity and stability of nickel-based catalysts,which are most widely used in alcohol SR processes due to their affordability and ability to break C–C,O–H and C–H bonds,yet are prone to rapid deactivation primarily caused by coke deposition and metal particle sintering.In this state-of-the-art review,a portfolio of strategies to improve the performance of Ni-based catalysts used in alcohol SR processes is unfolded with the intent of pinpointing the critical issues in catalyst development.Close examination of the literature reveals that the efforts tackling these recurring issues can be directed at the active metal,either by tuning Ni dispersion and Ni-support interactions or by targeting synergistic effects in bimetallic systems,while others focus on the support,either by modifying acid-base character,oxygen mobility,or by embedding Ni in specific crystallographic structures.This review provides a very useful tool to orient future work in catalyst development. 展开更多
关键词 H2 production Alcohol steam reforming ni-based catalysts catalyst development SINTERING Coke formation
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Effect of Ni Loading and Ce_(x)Zr_(1-x)O_(2) Promoter on Ni-Based SBA-15 Catalysts for Steam Reforming of Methane 被引量:7
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作者 Huijun Wan Xiujin Li +3 位作者 Shengfu Ji Bingyao Huang Kai Wang Chengyue Li 《Journal of Natural Gas Chemistry》 EI CAS CSCD 2007年第2期139-147,共9页
A series of Ni/SBA-15 catalysts with Ni contents ranging from 5wt% to 20wt% as well as 10wt%Ni/10wt%CexZr1-xO2/SBA-15 (x=0, 0.5, 1) were prepared. The structures of the catalysts were characterized using XRD, TPR, T... A series of Ni/SBA-15 catalysts with Ni contents ranging from 5wt% to 20wt% as well as 10wt%Ni/10wt%CexZr1-xO2/SBA-15 (x=0, 0.5, 1) were prepared. The structures of the catalysts were characterized using XRD, TPR, TEM and BET techniques. The catalytic activities of the catalysts for steam reforming of methane were evaluated in a continuous flow microreactor. The results indicated that both the Ni/SBA-15 and the Ni/CexZr1-xO2/SBA-15 catalysts had good catalytic activities at at- mospheric pressure. The 10wt%Ni/SBA-15 catalyst exhibited excellent stability at 800 ℃ for time on stream of 740 h. After the reaction, carbon deposits were not formed on the surface of the catalyst. There existed a regular hexagonal mesoporous structure in the Ni/SBA-15 and the Ni/CexZr1-xO2/SBA-15 catalysts. The nickel species and the CexZr1-xO2 component were all confined in the SBA-15 mesopores. The CexZr1-xO2 could promote dispersion of the nickel species in the Ni/CexZr1-xO2/SBA-15 catalysts. 展开更多
关键词 ni-based catalyst SBA-15 METHANE steam reforming SYNGAS
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Tuning the properties of Ni-based catalyst via La incorporation for efficient hydrogenation of petroleum resin 被引量:4
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作者 Qunhong Liu Jiangtao Yang +5 位作者 Hongwei Zhang Hongming Sun Shuzheng Wu Bingqing Ge Rong Wang Pei Yuan 《Chinese Journal of Chemical Engineering》 SCIE EI CAS CSCD 2022年第5期41-50,共10页
The hydrogenation of petroleum resin(PR)is an effective process to prepare high value-added hydrogenated PR(HPR).However,the preparation of non-noble metal-based catalysts with high catalytic activity for PR hydrogena... The hydrogenation of petroleum resin(PR)is an effective process to prepare high value-added hydrogenated PR(HPR).However,the preparation of non-noble metal-based catalysts with high catalytic activity for PR hydrogenation still remains a challenge.Herein,a La promoted Ni-based catalyst is reported through the thermal reduction of quaternary Ni La Mg Al-layered double hydroxides(Ni La Mg Al-LDHs).The incorporation of La is beneficial to the reduction and stability of Ni particles with reduced particle size,and the increased alkalinity effectively mitigates the breakage of molecular chains of PR.As a result,the La promoted Ni-based catalyst exhibits high catalytic activity and excellent stability for PR hydrogenation.A hydrogenation degree of 95.4%and 96.1%can be achieved for HC_(5)PR and HC_(9) PR with less reduced softening point,respectively.Notably,the hydrogenation degree still maintains at 92.7%even after 100 hours’reaction,much better than that without La incorporation or prepared using conventional impregnation method. 展开更多
关键词 ni-based catalyst Layered double hydroxides Promotion effect Petroleum resin HYDROGENATION
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Effect of Cu promoter on Ni-based SBA-15 catalysts for partial oxidation of methane to syngas 被引量:4
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作者 Fabien Habimana Xiujin Li +3 位作者 Shengfu Ji Bao Lang Daoan Sun Chengyue Li 《Journal of Natural Gas Chemistry》 EI CAS CSCD 2009年第4期392-398,共7页
A series of Ni/SBA-15 catalysts with 5wt% to 15wt% Ni content as well as a series of 12.5%Ni/Cu/SBA-15 catalysts with 1% to 10% copper content were prepared by the impregnation method. The catalytic performance for pa... A series of Ni/SBA-15 catalysts with 5wt% to 15wt% Ni content as well as a series of 12.5%Ni/Cu/SBA-15 catalysts with 1% to 10% copper content were prepared by the impregnation method. The catalytic performance for partial oxidation of methane was investigated in a continuous flow microreactor under atmospheric pressure. The textural and chemical properties of the catalysts were characterized by XRD, TEM, BET and Hz-TPR techniques. The results indicated that the catalysts modified with Cu promoter showed better performance than those without modification. For the 12.5%Ni/2.5%/Cu/SBA-15 catalyst, at 850 ℃ the conversion of CH4 reached 97.9% and the selectivity of CO and H2 reached 98.0% and 96.0%, respectively. In XRD patterns of the Ni/Cu/SBA-15 catalyst with 7.5 to 10% Cu contents there were CuO characteristic peaks beside NiO characteristic peaks. The mesoporous structure of SBA-15 was retained in all of the catalysts. TPR analysis of the catalysts revealed that a strong interaction between Ni, Cu promoter and SBA-15 support may be existed. This interaction enhanced significantly the redox properties of the catalysts resulting in the higher catalytic activity. 展开更多
关键词 Cu promoter ni-based catalyst SBA-15 METHANE partial oxidation of methane
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Active straining engineering on self-assembled stacked Ni-based hybrid electrode for ultra-low overpotential
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作者 Shujie Liu Rui-Ting Gao +3 位作者 Xianhu Liu Xueyuan Zhang Limin Wu Lei Wang 《Journal of Energy Chemistry》 SCIE EI CAS CSCD 2023年第2期217-226,I0006,共11页
Generating sufficient strains on metal surfaces are highly challenging owing to that most metals can deform plastically to relax the strains on the surfaces.In this work,we developed a facile but highly efficient stac... Generating sufficient strains on metal surfaces are highly challenging owing to that most metals can deform plastically to relax the strains on the surfaces.In this work,we developed a facile but highly efficient stacked deposition strategy to in situ activation and reconstruction of NiO/NiOOH on Ni matrix,following with the migration of Fe ions to NiOOH.The Fe sites on the Ni/NiO/NiOOH facilitate the formation of the stable*OH oxygenated intermediates,and the Ni matrix in the catalyst provides the catalyst excellent stability.The oxygen evolution reaction(OER)performance of the stacked NiFe-5 with compressive strain displays the strengthened binding to oxygenated intermediates and superior OER activity,the ultralow overpotentials of 162 versus reversible hydrogen electrode at 10 mA cm^(-2).On the other hand,the Ni-5 without the incorporation of Fe has shown an outstanding hydrogen evolution reaction(HER)activity,affording an overpotential of 47 mV at 10 mA cm^(-2).The NiFe-5‖Ni-5 enables the overall water splitting at a voltage of 1.508 V to achieve 20 mA cm^(-2) with remarkable durability.The stacked deposition strategy improves binding strength of Ni-based catalysts to oxygenated intermediates via generating compressive strain,causing high catalytic activities on OER and HER. 展开更多
关键词 ni-based catalysts Self-assembly stacked structure Ultra-low overpotential Water splitting
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Effect of MgO promoter on Ni-based SBA-15 catalysts for combined steam and carbon dioxide reforming of methane 被引量:3
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作者 Bingyao Huang Xiujin Li +3 位作者 Shengfu Ji Bao Lang Fabien Habimana Chengyue Li 《Journal of Natural Gas Chemistry》 EI CAS CSCD 2008年第3期225-231,共7页
A series of Ni/SBA-15 catalysts with Ni contents ranging from 5 wt% to 15 wt%, as well as another series of 10%Ni/MgO/SBA-15 catalysts, in which the range of the MgO content was from 1 wt% to 7 wt%, were prepared, and... A series of Ni/SBA-15 catalysts with Ni contents ranging from 5 wt% to 15 wt%, as well as another series of 10%Ni/MgO/SBA-15 catalysts, in which the range of the MgO content was from 1 wt% to 7 wt%, were prepared, and their catalytic performances for the reaction of combined steam and carbon dioxide reforming of methane were investigated in a continuous flow microreactor. The structures of the catalysts were characterized using the XRD, H2-TPR and CO2-TPD techniques. The results indicated that the CO selectivity for this reaction was very close to 100%, and the H2/CO ratio of the product gas could be controlled by changing the H2O/CO2 molar ratio of the feed gas. The simultaneous and plentiful existing of steam and CO2 had a significant influence on the catalytic performance of the 10%Ni/SBA-15 catalyst without modification. After reacting at 850 °C for 120 h over this catalyst, the CH4 conversion dropped from 98% to 85%, and the CO2 conversion decreased from 86% to 53%. However, the 10%Ni/3%MgO/SBA-15 catalyst exhibited a much better catalytic performance, and after reacting for 620 h, the CO2 conversion over this catalyst dropped from 92% to around 77%, while the CH4 conversion was not decreased. Oxidation of the Ni0 species as well as carbon deposition during the reaction were the main reasons for the deactivation of the catalyst without modification. On the other hand, modification by the MgO promoter improved the dispersion of the Ni0 species, and enhanced the CO2 adsorption affinity which in turn depressed the occurring of carbon deposition, and thus retarded the deactivation process. 展开更多
关键词 MgO promoter ni-based catalyst SBA-15 methane combined steam carbon dioxide reforming synthesis gas
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Effect of O_2 and H_2O on the tri-reforming of the simulated biogas to syngas over Ni-based SBA-15 catalysts 被引量:2
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作者 Daoan Sun Xiujin Li +1 位作者 Shengfu Ji Lingyan Cao 《Journal of Natural Gas Chemistry》 EI CAS CSCD 2010年第4期369-374,共6页
A series of Ni/SBA-15 catalysts with Ni contents from 7.5 wt% to 15 wt% were prepared by impregnation method.The effect of O2 and H2O on the combined reforming of the simulated biogas to syngas was investigated in a c... A series of Ni/SBA-15 catalysts with Ni contents from 7.5 wt% to 15 wt% were prepared by impregnation method.The effect of O2 and H2O on the combined reforming of the simulated biogas to syngas was investigated in a continuous flow fixed-bed micro-reactor.The stability of the catalyst was tested at 800 ?C.The results indicated that 10wt%Ni/SBA-15 catalyst exhibited the highest catalytic activities for the combined reforming of the simulated biogas to syngas.Under the reaction conditions of the feed gas molar ratios CH4/CO2/O2/H2O = 2/1/0.6/0.6,GHSV = 24000 ml·gcat^-1·h^-1 and the reaction temperature T = 800 ℃,the conversions of CH4 and CO2 were 92.8% and 76.3%,respectively,and the yields of CO and H2 were 99.0% and 82.0%,respectively.The catalytic activities of the catalyst did not decrease obviously after 100 h reaction time on stream. 展开更多
关键词 BIOGAS REFORMING SYNGAS oxygen steam ni-based catalyst SBA-15
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Studies on Catalysis in Partial Oxidation of Methane to Syngas(Ⅰ)──Performance and Characterization of Ni-based Catalysts 被引量:2
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作者 CHEN Ping ZHANG Hong-bin LIN Guo-dong and TSAI Khi-rui (Department of Chemistry &. State Key Laboratory for Physical Chemistry of the Solid Surface, Xiamen University, Xiamen, 361005) 《Chemical Research in Chinese Universities》 SCIE CAS CSCD 1996年第1期70-80,共11页
Highly active and selective Ni-based catalysts for partial oxidation of methane (POM) to syngas (CO/H,) have been studied and developed. Spectroscopic characterization by XRD, XPS, EPR, etc. demonstrated that under th... Highly active and selective Ni-based catalysts for partial oxidation of methane (POM) to syngas (CO/H,) have been studied and developed. Spectroscopic characterization by XRD, XPS, EPR, etc. demonstrated that under the POM reaction conditions, the Ni-components of the catalysts investigated were reduced and enriched on the surface to form metallic Ni0-phase. A comparative study of the first series of transition-metals showed that only Ni and Co have a high POM activity and selectivity, whereas the others (including Mn, Fe, Cu, etc. ) give mainly complete combustion products, Co, and H2O. The results favor the following viewpoints: the PoM activity is related with the rapidly changeable valence transitionmetal sites, M0/M2+ (e. g. Ni0/Ni2+ ), on the surface of the functioning catalysts;the transition-metal sites in zero-valence state seem to be responsible for the activation and dehydrogenation of methane by homolytic splitting of its C-H bonds on these sites. and the nature of rapidly changeable valence of the active sties is requisite for activation and rapid conversion of dioxygen. 展开更多
关键词 Partial oxidation of methane SYNGAS ni-based catalysts
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Optimizing the oxide support composition in Pr-doped CeO_(2) towards highly active and selective Ni-based CO_(2) methanation catalysts 被引量:2
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作者 Anastasios I.Tsiotsias Nikolaos D.Charisiou +9 位作者 Ayesha AlKhoori Safa Gaber Vlad Stolojan Victor Sebastian Bart van der Linden Atul Bansode Steven J.Hinder Mark A.Baker Kyriaki Polychronopoulou Maria A.Goula 《Journal of Energy Chemistry》 SCIE EI CAS CSCD 2022年第8期547-561,I0015,共16页
In this study,Ni catalysts supported on Pr-doped Ce O_(2) are studied for the CO_(2) methanation reaction and the effect of Pr doping on the physicochemical properties and the catalytic performance is thoroughly evalu... In this study,Ni catalysts supported on Pr-doped Ce O_(2) are studied for the CO_(2) methanation reaction and the effect of Pr doping on the physicochemical properties and the catalytic performance is thoroughly evaluated.It is shown,that Pr^(3+)ions can substitute Ce^(4+)ones in the support lattice,thereby introducing a high population of oxygen vacancies,which act as active sites for CO_(2) chemisorption.Pr doping can also act to reduce the crystallite size of metallic Ni,thus promoting the active metal dispersion.Catalytic performance evaluation evidences the promoting effect of low Pr loadings(5 at%and 10 at%)towards a higher catalytic activity and lower CO_(2) activation energy.On the other hand,higher Pr contents negate the positive effects on the catalytic activity by decreasing the oxygen vacancy population,thereby creating a volcano-type trend towards an optimum amount of aliovalent substitution. 展开更多
关键词 Power-to-gas CO_(2)methanation ni-based catalyst Pr-doped CeO_(2) Oxygen vacancy Catalytic activity Activation energy
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Catalytic steam reforming of biomass over Ni-based catalysts: Conversion from poplar leaves to hydrogen-rich syngas 被引量:1
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作者 Lingyan Cao Zhigang Jia Shengfu Ji Jinyong Hu 《Journal of Natural Gas Chemistry》 EI CAS CSCD 2011年第4期377-383,共7页
A series of Ni/SBA-15 catalysts with Ni contents from 5 wt%–20 wt%and CaO-12.5%Ni/SBA-15 catalysts with CaO contents from 1.4 wt%– 9.8 wt%have been prepared.The structure of the catalysts was characterized using X-r... A series of Ni/SBA-15 catalysts with Ni contents from 5 wt%–20 wt%and CaO-12.5%Ni/SBA-15 catalysts with CaO contents from 1.4 wt%– 9.8 wt%have been prepared.The structure of the catalysts was characterized using X-ray diffraction(XRD),N2 adsorption-desorption,transmission electron microscopy(TEM)and X-ray photoelectron spectroscopy(XPS).The performance of catalytic steam reforming of the poplar leaves to the hydrogen-rich syngas was tested in a fixed-bed reactor.The results indicate that the 7.0wt%CaO-12.5wt%Ni/SBA-15 catalyst exhibits the best performance for the catalytic steam reforming of poplar leaves to hydrogen-rich syngas.The ratio of H2:CO can reach ca 5:1 in the hydrogen-rich syngas.The yield of H2 can reach 273.30 mL/g(poplar leaves).In the CaO-Ni/SBA-15 catalyst,Ni active component mainly fills the role of catalytic steam reforming of the poplar leaves,and CaO active component mainly plays the role as water-gas shift and CO2 sorbent. 展开更多
关键词 BIOMASS steam reforming hydrogen-rich syngas ni-basic catalyst CAO
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Promotional effects of Ru and Fe on Ni/ZrO_(2) catalyst during CO_(2) methanation:A comparative evaluation of the mechanism
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作者 Jie Ren Feng Zeng +2 位作者 Chalachew Mebrahtu Zhandong Wang Regina Palkovits 《Journal of Energy Chemistry》 SCIE EI CAS CSCD 2023年第11期351-361,I0008,共12页
Ni-based catalysts are widely investigated non-noble metal-based systems for CO_(2)methanation.However,their industrial application is still limited due to lower activity at low-temperature and catalyst deactivation.I... Ni-based catalysts are widely investigated non-noble metal-based systems for CO_(2)methanation.However,their industrial application is still limited due to lower activity at low-temperature and catalyst deactivation.Incorporating a second metal such as Ru and Fe is considered as a successful strategy to overcome these challenges through alloy formation or the synergies provided by the interplay of two adjacent metallic sites.Nonetheless,their promotional effect on the CO_(2)methanation mechanism under similar conditions has not been reported yet.In this work,Fe and Ru-promoted Ni/ZrO_(2)catalysts were investigated to evaluate their promotional effect on the mechanism.The Ni/Fe ratio was first optimized and a CO_(2)conversion rate of 37.7 mmolCO_(2)/(molNi+Fes)and 96.3%CH^(4)selectivity was obtained over the Ni_(0.8)Fe_(0.2)/ZrO_(2)catalyst.In comparison with Ni_(0.8)Fe_(0.2)/ZrO_(2),Ni_(0.8)Ru_(0.2)/ZrO_(2)prepared with the same composition showed higher activity and stability in CO_(2)methanation.Characterization results indicate alloys formation and H spillover for Ni_(0.8)Ru_(0.2)/ZrO_(2)to be responsible for promotion.Besides,in situ DRIFTS studies evidenced the occurrence of both CO_(2)dissociative and associative pathways over Ni_(0.8)Ru_(0.2)/ZrO_(2)catalyst,while solely the CO_(2)associative pathway occurred for Ni_(0.8)Fe_(0.2)/ZrO_(2) 展开更多
关键词 ni-based catalyst Alloy formation H spillover CO_(2) methanation Methanation mechanism
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改性凹凸棒土的制备及其催化解吸CO_(2)性能研究
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作者 许腾 黄鑫 汪黎东 《应用化工》 CAS CSCD 北大核心 2024年第1期63-66,70,共5页
为进一步降低碳捕集技术成本,提高CO_(2)解吸效率,制备了一种低成本的金属改性凹凸棒土(ATP)固体酸催化剂,通过调控催化剂酸位丰度促进胺溶剂再生速率。结果表明,ATP-Zr可将CO_(2)解吸量和解吸速率分别提升13.8%和42%。此外,对合成的催... 为进一步降低碳捕集技术成本,提高CO_(2)解吸效率,制备了一种低成本的金属改性凹凸棒土(ATP)固体酸催化剂,通过调控催化剂酸位丰度促进胺溶剂再生速率。结果表明,ATP-Zr可将CO_(2)解吸量和解吸速率分别提升13.8%和42%。此外,对合成的催化剂进行了表征分析以及成型工艺的研究,可为固体酸催化剂制备及低能耗CO_(2)捕集技术的工业化应用提供理论支撑。 展开更多
关键词 碳捕集 催化剂 CO_(2)解吸 凹凸棒土 成型
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多级孔铁氮掺杂生物炭催化剂的制备及性能
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作者 林逸宁 葛强 +5 位作者 万金泉 朱丛韵 王艳 周贤波 刘宽勇 刘和芳 《化工环保》 CAS CSCD 北大核心 2024年第4期546-553,共8页
在水稻秸秆基铁氮掺杂生物炭粉末催化剂的基础上,制备了多级孔铁氮掺杂生物炭成型固体催化剂,探讨了其成型工艺,对其进行了表征,并对其活化过硫酸盐降解有机污染物的性能进行了评价,为铁氮掺杂生物炭催化剂的工业放大提供参考。该方法... 在水稻秸秆基铁氮掺杂生物炭粉末催化剂的基础上,制备了多级孔铁氮掺杂生物炭成型固体催化剂,探讨了其成型工艺,对其进行了表征,并对其活化过硫酸盐降解有机污染物的性能进行了评价,为铁氮掺杂生物炭催化剂的工业放大提供参考。该方法制备的成型球体催化剂具有良好的力学性能、丰富的多级孔结构、极低的铁离子浸出,可在宽pH范围内有效去除实际废水COD以及三氯苯酚(TCP)、双酚A(BPA)等有机污染物,可通过浸渍和热处理再生。吸附60 min、降解100 min后,COD、TCP、BPA的去除率分别可达46.85%、63.62%、90.18%。Fe^(2+)、Fe^(0)能够活化过硫酸盐产生·OH、SO_(4)^(-)·、·O_(2)^(-)和^(1)O_(2)降解有机污染物,Fe—N、C=O、O=C—OH和π→π^(*)位点作为电子供体,氧化态N作为电子受体。 展开更多
关键词 铁氮掺杂生物炭 催化剂成型 过硫酸盐高级氧化 造孔
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纤维基离子液多酸催化剂的合成及其超深快速脱硫性能研究
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作者 董兆琪 薛丽丽 +3 位作者 李壮壮 吴嘉琪 李斯文 王伟 《应用化工》 CAS CSCD 北大核心 2024年第9期2089-2094,共6页
采用浸渍法将Keggin型P-Mo-W多金属氧酸盐(POM)与双离子液体结合在醋酸纤维素(CA)上,获得一种用于萃取氧化脱硫(EODS)的成型催化材料,采用响应面设计实验,探究温度、催化剂质量、氧硫比以及多酸负载量对脱硫的影响。研究表明,最佳脱硫... 采用浸渍法将Keggin型P-Mo-W多金属氧酸盐(POM)与双离子液体结合在醋酸纤维素(CA)上,获得一种用于萃取氧化脱硫(EODS)的成型催化材料,采用响应面设计实验,探究温度、催化剂质量、氧硫比以及多酸负载量对脱硫的影响。研究表明,最佳脱硫反应条件为:模拟柴油25 mL,催化剂0.16 g,温度63℃,氧硫比4.8,多酸负载量1.08,反应2 h,可将模拟燃油中99.2%的DBT脱除。 展开更多
关键词 多金属氧酸盐催化剂 成型纤维材料 超深快速萃取氧化脱硫 响应面法
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CuCe/2D-VMT成型催化剂CO-SCR脱硝性能研究
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作者 何双利 潘珂珂 +1 位作者 于锋 曹鹏 《当代化工研究》 CAS 2024年第4期1-5,共5页
采用共沉淀法和涂敷法制备了CuCe/2D-VMT成型催化剂,通过X射线衍射(XRD)、傅里叶变换红外光谱(FT-IR)、透射电子显微镜(TEM)、氢气程序升温还原(H_(2)-TPR)和X射线光电子能谱(XPS)等表征方法对催化剂的理化性质进行了表征,并在中试脱硝... 采用共沉淀法和涂敷法制备了CuCe/2D-VMT成型催化剂,通过X射线衍射(XRD)、傅里叶变换红外光谱(FT-IR)、透射电子显微镜(TEM)、氢气程序升温还原(H_(2)-TPR)和X射线光电子能谱(XPS)等表征方法对催化剂的理化性质进行了表征,并在中试脱硝装置中用真实烟气评价了其CO选择性催化还原(CO-SCR)脱硝活性。结果表明:制备过程中实现了铜铈均匀掺杂,蛭石提供了更多氧空位,更优的分散性和氧化还原性能提升了催化剂的脱硝活性。在真实烟气中,125℃时NO转化率达57%;260h的长期测试中,催化剂NO转化率没有明显下降,维持在55%左右,表明催化剂能够用于实际工程中。 展开更多
关键词 NO 成型催化剂 CO-SCR 真实烟气
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Methane reforming with CO_2 to syngas over CeO_2-promoted Ni/Al_2O_3-ZrO_2 catalysts prepared via a direct sol-gel process 被引量:2
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作者 Hansheng Li Hang Xu Jinfu Wang 《Journal of Natural Gas Chemistry》 EI CAS CSCD 2011年第1期1-8,共8页
CeO2-promoted Ni/Al2O3-ZrO2 (Ni/Al2O3-ZrO2-CeO2) catalysts were prepared by a direct sol-gel process with citric acid as gelling agent. The catalysts used for the methane reforming with CO2 was studied by infrared s... CeO2-promoted Ni/Al2O3-ZrO2 (Ni/Al2O3-ZrO2-CeO2) catalysts were prepared by a direct sol-gel process with citric acid as gelling agent. The catalysts used for the methane reforming with CO2 was studied by infrared spectroscopy (IR), thermal gravimetric analysis (TGA), microscopic analysis, X-ray diffraction (XRD) and temperature-programmed reduction (TPR). The catalytic performance for CO2 reforming of methane to synthesis gas was investigated in a continuous-flow micro-reactor under atmospheric pressure. TGA, IR, XRD and microscopic analysis show that the catalysts prepared by the direct sol-gel process consist of Ni particles with a nanostructure of around 5 nm and an amorphous-phase composite oxide support. There exists a chemical interaction between metallic Ni particles and supports, which makes metallic Ni well dispersed, highly active and stable. The addition of CeO2 effectively improves the dispersion and the stability of Ni particles of the prepared catalysts, and enhances the adsorption of CO2 on the surface of catalysts. The catalytic tests for methane reforming with CO2 to synthesis gas show that the Ni/Al2O3-ZrO2-CeO2 catalysts show excellent activity and stability compared with the Ni/Al2O3 catalyst. The excellent catalytic activity and stability of the Ni/Al2O3-ZrO2-CeO2 are attributed to the highly, uniformly and stably dispersed small metallic Ni particles, the high reducibility of the Ni oxides and the interaction between metallic Ni particles and the composite oxide supports. 展开更多
关键词 methane reforming with CO2 SYNGAS ni-based catalyst CEO2 sol-gel process
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Low-temperature dry reforming of methane tuned by chemical speciations of active sites on the SiO_(2) and γ-Al_(2)O_(3) supported Ni and Ni-Ce catalysts 被引量:2
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作者 Yimin Zhang Ruiming Zeng +4 位作者 Yun Zu Linhua Zhu Yi Mei Yongming Luo Dedong He 《Chinese Journal of Chemical Engineering》 SCIE EI CAS CSCD 2022年第8期76-90,共15页
The cognition of active sites in the Ni-based catalysts plays a vital role and remains a huge challenge in improving catalytic performance of low temperature CO_(2) dry reforming of methane(LTDRM).In this work,typical... The cognition of active sites in the Ni-based catalysts plays a vital role and remains a huge challenge in improving catalytic performance of low temperature CO_(2) dry reforming of methane(LTDRM).In this work,typical catalysts of SiO_(2) and γ-Al_(2)O_(3) supported Ni and Ni-Ce were designed and prepared.Importantly,the difference in the chemical speciations of active sites on the Ni-based catalysts is revealed by advanced characterizations and further estimates respective catalytic performance for LTDRM.Results show that larger[Ni0-]particles mixed with[Ni-O-Sin])species on the Ni/SiO_(2)(R)make CH_(4) excessive decomposition,leading to poor activity and stability.Once the Ce species is doped,however,superior activity(59.0%CH_(4) and 59.8%CO_(2) conversions),stability and high H_(2)/CO ratio(0.96)at 600℃ can be achieved on the Ni-Ce/SiO_(2)(R),in comparison with other catalysts and even reported studies.The improved performance can be ascribed to the formation of integral([Ni0_(n))]-[CeⅢ-□-CeⅢ])species on the Ni-Ce/SiO_(2)(R)catalyst,containing highly dispersed[Ni]particles and rich oxygen vacancies,which can synergistically establish a new stable balance between gasification of carbon species and CO_(2) dissocia-tion.With respect to Ni-Ce/γ-Al_(2)O_(3)(R),the Ni and Ce precursors are easily captured by extra-framework Al_(n)-OH groups and further form stable isolated([Ni0_(n))]-[Ni-O-Al_(n)])and[CeⅢ-O-Al_(n)]species.In such a case,both of them preferentially accelerate CO_(2) adsorption and dissociation,causing more car-bon deposition due to the disproportionation of superfuous CO product.This deep distinguishment of chemical speciations of active sites can guide us to further develop new efficient Ni-based catalysts for LTDRM in the future. 展开更多
关键词 CO_(2)dry reforming of methane LOW-TEMPERATURE ni-based catalysts Chemical speciations Reforming reaction mechanisms
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Revealing the roles of components in glucose selective hydrogenation into 1,2-propanediol and ethylene glycol over Ni-MnO_x-ZnO catalysts 被引量:1
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作者 Yifan Zan Gai Miao +3 位作者 Hao Wang Lingzhao Kong Yaping Ding Yuhan Sun 《Journal of Energy Chemistry》 SCIE EI CAS CSCD 2019年第11期15-19,共5页
MnOx-promoted Ni-based catalyst supported by ZnO was developed to selectively hydrogenate glucose into polyols in water at 523 K with a yield of 64.9%. Using glucose, sorbitol, glycerol and LA as the rawmaterials, the... MnOx-promoted Ni-based catalyst supported by ZnO was developed to selectively hydrogenate glucose into polyols in water at 523 K with a yield of 64.9%. Using glucose, sorbitol, glycerol and LA as the rawmaterials, the roles of nickel, ZnO and MnOx were investigated. The results show that nickel provided a new pathway of glucose to sorbitol and played an important role in the hydrogenation of C3 intermediates to 1,2-propanediol(1,2-PDO). The high yield of 1, 2-PDO was attributed to effective C–C bond cleavage performance of ZnO support promoted by MnOx. ZnO and MnOx contribute to the conversion of glycerol to lactic acid(LA) and LA to 1, 2-PDO, respectively. A concise pathway for hydrogenation of glucose over Ni-based catalyst was proposed. 展开更多
关键词 GLUCOSE Hydrogenation 1 2-Propanediol Ethylene GLYCOL ni-based catalyst
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Hydrogenolysis of organosolv hydrolyzed lignin over high-dispersion Ni/Al-SBA-15 catalysts for phenolic monomers 被引量:1
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作者 Ying Xu Pengru Chen +3 位作者 Wei Lv Chenguang Wang Longlong Ma Qi Zhang 《Chinese Journal of Chemical Engineering》 SCIE EI CAS CSCD 2021年第4期307-314,共8页
Efficiency and recycling of catalysts are important for the lignin hydrogenolysis to obtain phenolic monomers.In this work,a series of highdispersion Ni/AlSBA15 catalysts were prepared by a direct and effective prepar... Efficiency and recycling of catalysts are important for the lignin hydrogenolysis to obtain phenolic monomers.In this work,a series of highdispersion Ni/AlSBA15 catalysts were prepared by a direct and effective preparation method,and then used in the hydrogenolysis of diphenyl ether(DE)and organosolv hydrolyzed lignin(OHL)for phenolic monomers.The universality of asmade catalysts in different solvents and cyclic performance were investigated.Results showed that the addition of ethylene glycol(EG)during the loading process of Ni promoted the dispersion of metal efficiently.High dispersion of Ni species could highly enhance the conversion of DE and the OHL which Ni/AlSBA15(1EG)exhibited the excellent catalytic performance.Decalin was found to be most effective solvent on the conversion of DE(99.16%).84.77%liquefaction ratio and 21.36%monomer yield were achieved,and no obvious char was observed after the depolymerization of OHL in ethanol solvent at 280℃for 4 h over the Ni/AlSBA15(1EG)catalyst. 展开更多
关键词 LIGNIN Hydrogenolysis depolymerization High-dispersion ni-based catalyst Al-SBA-15
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Modeling and optimization of methane dry reforming over Ni-Cu/Al_2O_3 catalyst using Box-Behnken design 被引量:1
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作者 Seyedeh Molood Masoom Nataj Seyed Mehdi Alavi Golshan Mazloom 《Journal of Energy Chemistry》 SCIE EI CAS CSCD 2018年第5期1475-1488,共14页
In this work the effects of the contents of nickel (5, 7.5, 10 wt%) and copper (0, 1, 2 wt%) and reac- tion temperature (650, 700, 750 ℃) on the catalytic performance of Ni-Cu/Al_2O_3 catalyst in methane dry re... In this work the effects of the contents of nickel (5, 7.5, 10 wt%) and copper (0, 1, 2 wt%) and reac- tion temperature (650, 700, 750 ℃) on the catalytic performance of Ni-Cu/Al_2O_3 catalyst in methane dry reforming were evaluated using Box-Behnken design in order to optimize methane conversion, H_2/CO ratio and the catalyst deactivation. Different catalysts were prepared by co-impregnation method and characterized by XRD, BET, H_2-TPR, FESEM and TG/DTA analyses. The results revealed that copper addi- tion improved the catalyst reducibility. Promoted catalyst with low amounts of Cu gave higher activity and stability with high resistance to coke deposition and agglomeration of active phase especially during the reaction. However catalysts with high amounts of Cu were less active and rather deactivated due to the active sites sintering as well as Ni covering by Cu-enriched phase. The optimal conditions were de- termined by desirability function approach as 10 wt% of Ni, 0.83 wt% of Cu at 750℃. CH_4 conversion of 95.1%, H_2/CO ratio of 1 and deactivation of 1.4% were obtained experimentally under optimum conditions, which were in close agreement with the values oredicted hv the developed model. 展开更多
关键词 Methane dry reforming Copper addition ni-based catalyst SYNGAS Box-Behnken design
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