Zobrazeno 1 - 10
of 188
pro vyhledávání: '"Aguayo, A."'
Publikováno v:
Industrial & Engineering Chemistry Research. 61:10365-10376
Publikováno v:
Industrial & Engineering Chemistry Research. 59:14689-14702
The dimethyl ether (DME)-to-olefins (DTO) process is an interesting alternative to the methanol-to-olefins process because of the easier production of DME, its higher reactivity, and the moderate d...
Autor:
Zuria Tabernilla, José Valecillos, Enrique Sastre, Pedro Castaño, Andrés T. Aguayo, Eva Epelde
Publikováno v:
Industrial & Engineering Chemistry Research. 59:13892-13905
We proved that the disposition of tandem fixed-beds of ZSM-5 with SAPO-18 catalysts could decrease the deactivation of the second catalytic bed during the methanol-to-olefins (MTO) reaction. For th...
Publikováno v:
Industrial & Engineering Chemistry Research. 59:713-722
The intensification of CO2 valorization has been theoretically studied in the direct synthesis of dimethyl ether (DME) carried out in a packed-bed reactor by means of two strategies pursuing the at...
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Autor:
Javier Bilbao, Andrés T. Aguayo, Pedro Castaño, Ainara Ateka, Tomás Cordero-Lanzac, Paula Pérez-Uriarte
Publikováno v:
Industrial & Engineering Chemistry Research. 57:13689-13702
The impact of different process variables affecting the coking and rejuvenation of HZSM-5 zeolite catalyst has been studied during the conversion of dimethyl ether (DME) to olefins in a fixed bed reactor. Those variables involve the effect of (i) the
Publikováno v:
Industrial & Engineering Chemistry Research; 7/27/2022, Vol. 61 Issue 29, p10365-10376, 12p
Publikováno v:
Industrial & Engineering Chemistry Research. 57:1169-1178
Zr incorporation in the CuO-ZnO catalyst for methanol synthesis from CO+CO2 mixtures, for its later use in the bifunctional catalyst conformation for dimethyl ether (DME) direct synthesis, has been studied. Different Cu/Zn/Zr ratio catalysts were pre
Publikováno v:
Industrial & Engineering Chemistry Research. 57:908-919
The conversion of chloromethane into hydrocarbons over a HZSM-5 zeolite based catalyst is investigated with the aim of establishing a kinetic model suitable for simulating this process for indirect valorization of the methane contained in shale gas.
Publikováno v:
Industrial & Engineering Chemistry Research; July 2022, Vol. 61 Issue: 29 p10365-10376, 12p