Catalysis Science & Technology

Catalysis Science & Technology

Catalysis Science & Technology Accepted Manuscript This is an Accepted Manuscript, which has been through the Royal Society of Chemistry peer review process and has been accepted for publication. Accepted Manuscripts are published online shortly after acceptance, before technical editing, formatting and proof reading. Using this free service, authors can make their results available to the community, in citable form, before we publish the edited article. We will replace this Accepted Manuscript with the edited and formatted Advance Article as soon as it is available. You can find more information about Accepted Manuscripts in the Information for Authors. Please note that technical editing may introduce minor changes to the text and/or graphics, which may alter content. The journal’s standard Terms & Conditions and the Ethical guidelines still apply. In no event shall the Royal Society of Chemistry be held responsible for any errors or omissions in this Accepted Manuscript or any consequences arising from the use of any information it contains. www.rsc.org/catalysis Page 1 of 29 Catalysis Science & Technology Journal Name RSC Publishing ARTICLE Redox-stable chromate cathode decorated with in situ grown nickel nanocatalyst towards efficient carbon Cite this: DOI: 10.1039/x0xx00000x dioxide electrolysis Cong Ruan a and Kui Xie a, b * Manuscript Received 00th January 2012, Accepted 00th January 2012 DOI: 10.1039/x0xx00000x Redox-stable La 0.75 Sr 0.25 Cr 0.5 Mn 0.5 O3-δ (LSCM) ceramic can be utilized as a solid oxide www.rsc.org/ electrolyzer cathode for direct carbon dioxide electrolysis; nevertheless, the insufficient electro-catalytic activity of ceramic LSCM restricts the electrode performances and current efficiencies. In this paper, catalytic-active nickel nanoparticles are anchored on the surface of LSCM substrate through in situ growing process to improve electrode performances. The Accepted combined analyses of XRD, TEM, XPS, SEM and EDS demonstrate the reversible in situ growth of nickel catalyst by transforming A-site deficient and B-site excess (La 0.75 Sr 0.25 )0.9 (Cr 0.5 Mn 0.5 )0.9 Ni 0.1 O3-δ (LSCMN) to LSCM and nickel in redox cycles. The conductivities of LSCM and LSCMN are investigated and correlated with electrode performances in symmetrical cells and electrolysis cells. Significant improvement in electrode polarization resistance has been observed for the LSCMN cathode. The current efficiency is considerably improved by 30% with LSCMN in contrast to bare LSCM cathode for direct Technology carbon dioxide electrolysis at 800 ºC. & Introduction and the O 2- transports through electrolyte to anode to form Recently, solid oxide electrolyzer has been paid a lot of oxygen gas. 6,7 High operation temperatures ranging from 700 to attention because of its enormous advantages of efficient 1000 ºC are of great promise in the CO 2 electrolysis process for electrochemical conversion of CO 2 into fuels using renewable the reason that heat partly offers the energy for molecular Science electrical energy, which provides an alternative for producing dissociation which leads to favorable kinetics and 1–5 renewable fuels. High temperature CO 2 electrolysis in an thermodynamics even without using expensive noble metals as oxide-ion-conducting solid oxide electrolyzer is of great electrodes. 8,9 advantage because it can directly electrolyze CO 2 into CO and Traditional Ni-YSZ composite cathode has been widely oxygen under external voltages. In this process, the CO 2 is used in the oxide-ion-conducting solid oxide electrolyzers electrochemically reduced into CO and oxide ion at cathode because of its excellent performances for high temperature CO 2 Catalysis This journal is © The Royal Society of Chemistry 2013 J. Name ., 2013, 00 , 1-3 | 1 Catalysis Science & Technology Page 2 of 29 ARTICLE Journal Name electrolysis.3,10,11 Irvine et al. had investigated the Ni-YSZ Traditional Ni, Fe, Cu and etc. have been commonly composite cathode for CO 2 electrolysis in solid oxide utilized as excellent catalysts in many fields such as biogas electrolyzers, and found that the current density of 0.8 A·cm -2 reforming, water gas shift reaction and catalytic conversion of 22,23 had been achieved in CO 2/CO atmospheres under 2.25 V at 900 CO 2. Among these elements, nickel is a well-known ºC. 6 Barnett et al. had also performed coelectrolysis of catalyst for its excellent catalytic activity in heterogeneous 24,25 CO 2/H 2O using the solid oxide electrolyzers based on Ni-YSZ catalysis, electrochemistry and fuel cells. Caldes et al. had cathode and yielded a syngas production rate of about 7 achieved the improved electrochemical characteristics of the -2 sccm·cm in 25% H 2, 25% CO 2 and 50% H 2O under 1.3 V at electrodes doped with a small amount of nickel nanocatalyst. Manuscript 800 ºC. 12 It is obvious that a significant concentration of They found that the total conductivities of the nickel doped reducing gas is demanded to flow over the Ni-YSZ cathodes to LSCM-based materials had been improved to 36 S·cm -1 for -1 avoid the oxidation of nickel. The inherent redox instability of LSCM 0.44 N0.06 and 24 S·cm for LSC 0.44 MN 0.06 compared to 13 Ni-YSZ would lead to the loss of electronic conductivity and S·cm -1 of bare LSCM. 25 These metal nanocatalysts can be even the failure of the electrode, which has become the added into the electrode by impregnation with a metallic salt or limitation of electrode performances. 13,14 Recently, it has been a nanopowder suspension, or precipitating with metal nano- Accepted reported that the perovskite-type ceramic clusters on the electrode surface; besides, in situ growth of La 0.75 Sr 0.25 Cr 0.5 Mn 0.5 O3-δ (LSCM) is a promising cathode metal nanoparticles is also an alternative route to coat the material for its excellent redox stability and catalytic activity nanocatalyst onto the substrate.26 Irvine et al. had recently 15–18 compared to the traditional Ni-YSZ. Direct CO 2 reported that uniformly dispersed nanoparticles could be electrolysis with electrolyzers based on LSCM cathode has decorated on the surface by in situ growing the nanoparticles been investigated in previous works, promising electrode directly from the (porous) backbone support. They had performances and current efficiencies without the flow of demonstrated that the growing nano-size phases from Technology reducing gas over the cathode have been demonstrated.9,19 Yue perovskites can be controlled by tuning deviations from the & et al. had demonstrated the excellent performances of CO 2 ideal ABO 3 stoichiometry, such as A-site-deficient perovskites electrolysis in high temperature solid oxide electrolyzers based (A/B < 1). A-site deficiency would offer driving force for the on LSCM composite cathode, the CO production rate of B-site exsolution for the reason that in this system B-site approximately 1.2 µmol·s-1 and the Faraday efficiency of 96% exsolution tends to locally revert the perovskite towards a 26 Science had been obtained in CO 2/CO atmospheres under 1.0 V at 900 stable, ‘defect-free’ ABO 3 stoichiometry. ºC. 20 However, the cathode performances are restricted by the In this work, nickel is introduced into the B-site of LSCM insufficient electro-catalytic activity of LSCM. For this reason, lattice to form the A-site deficiency and B-site excess it is of great importance to enhance the electro-catalytic activity (La 0.75 Sr 0.25 )0.9 (Cr 0.5 Mn 0.5 )0.9 Ni 0.1 O3-δ (LSCMN). The crystal of the LSCM electrode in order to improve the performances of structures and reversible exsolution of nickel nanoparticles are 21 direct CO 2 electrolysis. investigated and correlated to the electrical properties of the Catalysis 2 | J. Name ., 2012, 00 , 1-3 This journal is © The Royal Society of Chemistry 2012 Page 3 of 29 Catalysis Science & Technology Journal Name ARTICLE samples. Direct CO 2 electrolysis is then investigated with powders with the binding energies calibrated to the C 1s peak at LSCM and LSCMN cathodes at 800 ºC, respectively. 285 eV. Experimental About 2.0 g LSCM or LSCMN powders were pressed into a bar followed with a heat treatment at 1400 ºC (2 ºC·min -1) for All the chemicals (99.9%) were bought from Sinopharm 10 h in air for the conductivity tests. The conductivity test was Chemical Reagent Co., Ltd (China) unless otherwise specified. operated through the DC four-terminal method with a LSCM or The LSCM powders were synthesized through a combustion LSCMN bar mounted by four Ag wires (0.4 mm in diameter) method with stoichiometric amounts of La 2O3, SrCO 3, using the conductive adhesive (DAD87, Shanghai Research Cr(NO 3)3·9H 2O, C 4H6MnO 4·4H 2O and glycine followed by a Manuscript Institute for Synthetic Resins, Shanghai, China) followed with a heat treatment at 1200 ºC (2 ºC·min -1) for 5 h in air as described heat treatment at 550 °C (3 ºC·min -1) for 30 min in air, and the elsewhere, and the LSCMN powders were synthesized through bar was connected to a four terminal jig coupled with an the same method as LSCM with extra NiO. 27,28 The oxygen sensor device. The conductivities of LSCM and (La 0.8 Sr 0.2 )0.95 MnO 3-δ (LSMO) powders were prepared through LSCMN versus temperature in air were measured from the same method as described above with stoichiometric approximately 200 to 800 °C (3 ºC·min -1) using an online amounts of La 2O3, SrCO 3, C 4H6MnO 4·4H 2O and glycine Accepted multi-meter (Keithley 2000, Digital Multimeter, Keithley followed by a heat treatment at 1100 ºC (2 ºC·min -1) for 3 h in 29 Instrument Inc., USA).

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