000121128 001__ 121128
000121128 005__ 20240319081007.0
000121128 0247_ $$2doi$$a10.1016/j.jiec.2022.05.045
000121128 0248_ $$2sideral$$a131543
000121128 037__ $$aART-2022-131543
000121128 041__ $$aeng
000121128 100__ $$0(orcid)0000-0002-6762-0971$$aSanz-Martínez, A.$$uUniversidad de Zaragoza
000121128 245__ $$aMethanol to gasoline (MTG): Parametric study and validation of the process in a two-zone fluidized bed reactor (TZFBR)
000121128 260__ $$c2022
000121128 5060_ $$aAccess copy available to the general public$$fUnrestricted
000121128 5203_ $$aMethanol to Gasoline (MTG) process transforms methanol to hydrocarbons within the boiling point range of gasoline. The result is a wide spectrum of products (olefins, paraffins, aromatics and naphthenics, among others), with the total conversion of methanol to hydrocarbons and water. Catalyst deactivation by coke is a main problem in this process. This work aims to determine the feasibility of carrying out the production of gasoline from methanol in a two-zone fluidized bed reactor (TZFBR). The hypothesis is that the formation of carbonaceous deposits (coke) on the catalyst particles can be counteracted by its combustion in the regeneration zone that this novel reactor presents, thus achieving stable and continuous operation. In this way, both processes (reaction and regeneration) would be being carried out simultaneously in the same reactor (process intensification). The comparison of results between a conventional fluidized bed reactor and a TZFBR shows that the second one actually provides a better stability over time.
000121128 536__ $$9info:eu-repo/grantAgreement/ES/MINECO/CTQ2016-76533-R$$9info:eu-repo/grantAgreement/ES/MINECO/PID2019-106196RB-I00
000121128 540__ $$9info:eu-repo/semantics/openAccess$$aby$$uhttp://creativecommons.org/licenses/by/3.0/es/
000121128 590__ $$a6.1$$b2022
000121128 592__ $$a1.005$$b2022
000121128 591__ $$aENGINEERING, CHEMICAL$$b23 / 141 = 0.163$$c2022$$dQ1$$eT1
000121128 593__ $$aChemical Engineering (miscellaneous)$$c2022$$dQ1
000121128 591__ $$aCHEMISTRY, MULTIDISCIPLINARY$$b46 / 178 = 0.258$$c2022$$dQ2$$eT1
000121128 594__ $$a11.1$$b2022
000121128 655_4 $$ainfo:eu-repo/semantics/article$$vinfo:eu-repo/semantics/publishedVersion
000121128 700__ $$0(orcid)0000-0002-7488-6196$$aLasobras, J.
000121128 700__ $$0(orcid)0000-0001-9022-2835$$aSoler, J.$$uUniversidad de Zaragoza
000121128 700__ $$0(orcid)0000-0003-1940-9597$$aHerguido, J.$$uUniversidad de Zaragoza
000121128 700__ $$0(orcid)0000-0002-2494-102X$$aMenéndez, M.$$uUniversidad de Zaragoza
000121128 7102_ $$15005$$2555$$aUniversidad de Zaragoza$$bDpto. Ing.Quím.Tecnol.Med.Amb.$$cÁrea Ingeniería Química
000121128 773__ $$g113 (2022), 189-195$$pJ. Ind. Eng. Chem.$$tJournal of Industrial and Engineering Chemistry$$x1226-086X
000121128 8564_ $$s894064$$uhttps://zaguan.unizar.es/record/121128/files/texto_completo.pdf$$yVersión publicada
000121128 8564_ $$s2974590$$uhttps://zaguan.unizar.es/record/121128/files/texto_completo.jpg?subformat=icon$$xicon$$yVersión publicada
000121128 909CO $$ooai:zaguan.unizar.es:121128$$particulos$$pdriver
000121128 951__ $$a2024-03-18-14:44:26
000121128 980__ $$aARTICLE