Zobrazeno 1 - 10
of 14
pro vyhledávání: '"Ding Ye Fang"'
Publikováno v:
Advanced Materials Research. :990-998
The conventional process for isobornyl acetate synthesis from camphene and acetic acid is a batch process. The purpose of this paper is to synthesize isobornyl acetate in continuous process in a fixed bed reactor. The continuous reaction conditions w
Publikováno v:
Applied Mechanics and Materials. :1547-1553
The effects of several factors, including fuel mixing ratio fed into boiler, bed temperature, primary air ratio, on burnout characteristics of mixed fuel of petroleum coke and oil shale were investigated at a 1 MW circulating fluidized bed (CFB) test
Publikováno v:
Advanced Materials Research. 132:246-256
A series of SAPO-34 materials were synthesized hydrothermally in the presence of mixed templating agent (named TEDE) of tetraethyl ammonium hydroxide (TEAOH) and diethylamine (DEA). The effects of template amount, SiO2/Al2O3 and P2O5/Al2O3 molar rati
Publikováno v:
Advanced Materials Research. 132:257-263
With incipient impregnation method, cobalt-based catalysts were prepared. The effects of the ZrO2 modification of support and the addition of the second metal Ru on heavy hydrocarbon synthesis were investigated in a fixed-bed reactor. The results rev
A Ni-based catalyst supported by γ-Al2O3 was prepared by impregnation method, and the catalyst was used in a low CO and CO2 concentration methanation system. The effect of temperature, pressure and space velocity on the methanation reaction was inve
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_dedup___::41791a101536cf45a2fce09b297ae935
Radial flow reactor was focused for large scale methanol synthesis and in which the heat transfer type was cross-flow. The effects of operating conditions including the reactor inlet air temperature, the heating pipe temperature and the air flow rate
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_dedup___::3dcdd6c0c44c1cda809d56caf265e76d
Dehydration of methanol to dimethyl ether (DME) over a commercial Al2O3 catalyst was studied in an isothermal integral fixed bed reactor. The experiments were performed on the temperature interval 513-613 K, liquid hourly space velocity (LHSV) of 0.9
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_dedup___::7edd184890c2bbdc5ce969273c65efcd
Methanol-to-olefins coupled with transformation of coal or natural gas to methanol gives an interesting and promising way to produce ethylene and propylene. To investigate solid concentration in gas-solid fluidized bed for methanol-to-olefins process
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_dedup___::9de83c058bafa52df5ebb5545d415923
Methanol-to-olefins (MTO) coupled with transformation of coal or natural gas to methanol gives an interesting and promising way to produce ethylene and propylene. To investigate solid concentration in gas-solid fluidized bed for methanol-to-olefins p
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_dedup___::683595180df691e072c329c6816e94eb
Publikováno v:
ACS Symposium Series ISBN: 9780841238275
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::ab0041230cd49f6ec45befe9538ff816
https://doi.org/10.1021/bk-2003-0852.ch010
https://doi.org/10.1021/bk-2003-0852.ch010