Correlating metal poisoning with zeolite deactivation in an individual catalyst particle by chemical and phase-sensitive X-ray microscopy.
Correlating metal poisoning with zeolite deactivation in an individual catalyst particle by chemical and phase-sensitive X-ray microscopy.
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DOI:
10.1002/anie.201210030
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发表时间:
2013-06-03
影响因子:
16.6
通讯作者:
Weckhuysen, Bert M.
中科院分区:
文献类型:
--
作者:
Ruiz-Martinez, Javier;Beale, Andrew M.;Deka, Upakul;O'Brien, Mathew G.;Quinn, Paul D.;Mosselmans, J. Fred W.;Weckhuysen, Bert M.
Chemical industries heavily rely on the use of heterogeneous catalysts. The development of more sustainable chemical processes requires, however, better catalyst formulations and ultimately tailoring of these catalytic materials for a specific application. A showcase example is fluid catalytic cracking (FCC), which is industrially applied to convert heavy oil fractions into more valuable chemicals, such as gasoline and olefins.[1] The detrimental effect of metals originating from crude oil, especially Ni and V, on FCC catalysts is widely recognized.[2] The metals damage the active zeolite phase, being either ultrastable zeolite Y (USY) or zeolite ZSM-5. As a result, pore accessibility and acidity are decreased, while dehydrogenation–hydrogenation reactions are favored, leading to increased coke formation. In the case of Ni, the main detrimental effect is coke formation,[3] while V poisoning is associated with permanent zeolite damage in the presence of steam at high temperatures.[2a] Several research groups have attempted to understand the mechanism of metal poisoning by observing the distribution of metals across the 50–150 mm FCC catalyst particle and between the different catalyst components; that is, zeolite, matrix (for example, alumina and clay), and additives, which comprise the FCC catalyst particle. Such characterization studies have been mostly conducted with invasive characterization methods.[4] These investigations revealed that V is much more mobile than Ni and proceeds more quickly towards the interior of the FCC catalyst particle.[4d] The mayor drawback with these previous studies is that they require an invasive preparation step, where the FCC catalyst particle is cut along the desired plane of analysis. This bisection is far from trivial and in most of the cases an alteration in the distribution of the distinct FCC components is observed. Therefore, a non-invasive approach can be expected to deliver more truthful information about the location of metal poisons. Furthermore, the relationship between metal poisoning and zeolite deactivation is not well understood, and to date there are no studies providing detailed information about the effect of deactivation on the crystalline zeolite structure within an individual FCC catalyst particle.Herein we report for the first time the detrimental effect of metal poisons on the zeolitic material after deactivation in a commercial FCC unit at the level of a single catalyst particle. Using synchrotron-based hard X-ray radiation, the presence of Ni, V, as well as the crystalline phases can be determined with micrometre resolution in 2D or 3D. Furthermore, the non-invasive nature of the experimental approach avoids the pre-bisection of the FCC particle, avoiding damage and contamination to the catalyst material. Our findings lead to a better understanding of the deactivation processes taking place in real-life FCC catalysis and open the possibility to apply this approach for the study of other important catalytic materials, comprising both metals and crystalline phases.
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影响因子:
--
作者:
Beale, Andrew M.;Paul, Michael;Fowles, Martin
通讯作者:
Fowles, Martin
影响因子:
4.3
作者:
Buurmans, Inge L. C.;Ruiz-Martinez, Javier;Weckhuysen, Bert M.
通讯作者:
Weckhuysen, Bert M.
影响因子:
19
作者:
Basile, Francesco;Benito, Patricia;Vaccari, Angelo
通讯作者:
Vaccari, Angelo
影响因子:
5.5
作者:
Escobar, Alyne S.;Pinto, Fernanda V.;Pereira, Marcelo M.
通讯作者:
Pereira, Marcelo M.
影响因子:
7.3
作者:
KUGLER, EL;LETA, DP
通讯作者:
LETA, DP