000070811 001__ 70811
000070811 005__ 20200221144300.0
000070811 0247_ $$2doi$$a10.1016/j.cattod.2016.02.063
000070811 0248_ $$2sideral$$a97513
000070811 037__ $$aART-2016-97513
000070811 041__ $$aeng
000070811 100__ $$0(orcid)0000-0001-6360-4475$$aLatorre, N.$$uUniversidad de Zaragoza
000070811 245__ $$aGrowth of carbonaceous nanomaterials over stainless steel foams. Effect of activation temperature
000070811 260__ $$c2016
000070811 5060_ $$aAccess copy available to the general public$$fUnrestricted
000070811 5203_ $$aSome of the problems that occur during the operation of chemical reactors based of structured catalytic substrates, as monoliths, foams, membranes, cloths, fibres and other systems, are related to the preparation of long term stable coatings. Frequently, the deposition of the catalytic layer is carried out by washcoating, requiring this step a cautious attention, especially in the case of complex geometries, like of that of foams or cloths. In the case of the deposition of layers of carbonaceous materials (CNMs), an alternative route, avoiding the washcoating, it is their direct growth by catalytic decomposition light hydrocarbons (also called CCVD), over the surface of the metallic substrate. In this case, if the metallic substrate is of stainless steel, it already contains the catalytic active phases like Fe and Ni. In order to optimize the process of CNMs growth over structured metallic substrates, we are studying the effect of the main operational variables of the ethane decomposition reaction on stainless steel foams. In this contribution we present a study of the influence of the temperature of the activation (oxidation and reduction) stage on the type and morphology of the carbonaceous materials formed. The results obtained allow us to determine the optimal operating conditions to maximize the amount and the selectivity of the process to obtain a given type of CNM.
000070811 536__ $$9info:eu-repo/grantAgreement/ES/MINECO/ENE2013-47880-C3-1-R
000070811 540__ $$9info:eu-repo/semantics/openAccess$$aby-nc-nd$$uhttp://creativecommons.org/licenses/by-nc-nd/3.0/es/
000070811 590__ $$a4.636$$b2016
000070811 591__ $$aCHEMISTRY, APPLIED$$b6 / 72 = 0.083$$c2016$$dQ1$$eT1
000070811 591__ $$aENGINEERING, CHEMICAL$$b12 / 135 = 0.089$$c2016$$dQ1$$eT1
000070811 591__ $$aCHEMISTRY, PHYSICAL$$b30 / 145 = 0.207$$c2016$$dQ1$$eT1
000070811 592__ $$a1.322$$b2016
000070811 593__ $$aChemistry (miscellaneous)$$c2016$$dQ1
000070811 593__ $$aCatalysis$$c2016$$dQ2
000070811 655_4 $$ainfo:eu-repo/semantics/article$$vinfo:eu-repo/semantics/acceptedVersion
000070811 700__ $$0(orcid)0000-0001-9220-9909$$aCazaña, F.
000070811 700__ $$0(orcid)0000-0002-6873-5244$$aSebastian, V.$$uUniversidad de Zaragoza
000070811 700__ $$0(orcid)0000-0002-5713-1402$$aRoyo, C.$$uUniversidad de Zaragoza
000070811 700__ $$0(orcid)0000-0002-2363-2735$$aRomeo, E.$$uUniversidad de Zaragoza
000070811 700__ $$aCenteno, M. A.
000070811 700__ $$0(orcid)0000-0002-7836-5777$$aMonzón, A.$$uUniversidad de Zaragoza
000070811 7102_ $$15005$$2555$$aUniversidad de Zaragoza$$bDpto. Ing.Quím.Tecnol.Med.Amb.$$cÁrea Ingeniería Química
000070811 773__ $$g273 (2016), 41-49$$pCatal. today$$tCatalysis Today$$x0920-5861
000070811 8564_ $$s947764$$uhttps://zaguan.unizar.es/record/70811/files/texto_completo.pdf$$yPostprint
000070811 8564_ $$s68623$$uhttps://zaguan.unizar.es/record/70811/files/texto_completo.jpg?subformat=icon$$xicon$$yPostprint
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000070811 951__ $$a2020-02-21-13:32:02
000070811 980__ $$aARTICLE