Zobrazeno 1 - 10
of 18
pro vyhledávání: '"Wugeng Liang"'
Autor:
James Lowrey, Aghaddin Mamedov, David West, Sagar Sarsani, Perez Hector, Wugeng Liang, Istvan Lengyel
Publikováno v:
Catalysis Today. 299:60-66
Layered loading of catalysts with different catalytic properties is studied for oxidative coupling of methane reaction (OCM) in a fixed bed reactor. Layered loading of a more active catalyst Ag-Mn-Na2WO4/SiO2 in front of a more selective one Ce-Mn-Na
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::6d337d5ac23f31b6e99e4fb327d15110
https://doi.org/10.1016/j.cattod.2017.03.058
https://doi.org/10.1016/j.cattod.2017.03.058
Publikováno v:
Chemical Engineering Journal. 328:484-496
We report the exploitation of thermal effects and bifurcation (ignition and extinction) behavior to enable steady-state operation of an Oxidative Coupling of Methane (OCM) reactor with ambient feed and furnace temperature. Using a simplified kinetic
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::a165cd92693f7b0103605d352a70758b
https://doi.org/10.1016/j.cej.2017.07.002
https://doi.org/10.1016/j.cej.2017.07.002
Autor:
Jingxu Zhu, Wugeng Liang
Publikováno v:
Chemical Engineering Journal. 68:51-62
A core-annulus model is developed to describe the radial nonuniform flow structure in a liquid-solid circulating fluidized bed (LSCFB). Good agreement is obtained between the model predictions and the experimental results of the radial distributions
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::2e4d38e0496c591d1393ae41ba04bc23
https://doi.org/10.1016/s1385-8947(97)00065-x
https://doi.org/10.1016/s1385-8947(97)00065-x
Publikováno v:
Industrial & Engineering Chemistry Research. 36:1882-1886
Diffusion coefficients reported for zeolites have ranged over a wide span of magnitude depending on methods of measurement. We have analyzed determinations made by various investigators and methods on a number of zeolites and guest molecules. When im
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::d96527d11c6d8cc22465debaba368c93
https://doi.org/10.1021/ie960493+
https://doi.org/10.1021/ie960493+
Publikováno v:
Powder Technology. 90:95-102
A new fluidization regime, the circulating fluidization regime, is identified for the upwards liquid–solid fluidization operation. This circulating fluidization regime is characterized by non-uniform radial distribution of liquid velocity, particle
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::29da565b4ff6be08128335a8a5aade06
https://doi.org/10.1016/s0032-5910(96)03198-1
https://doi.org/10.1016/s0032-5910(96)03198-1
Publikováno v:
Chemical Engineering & Technology. 19:456-461
A new reactive distillation device, the multistage gas/liquid/solid three-phase fluidized bed, has been developed. The flow regimes of the multistage three-phase fluidized bed have been studied and the regimes can be divided into the liquid leakage r
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::ed09d82d083d097b51bf905ac71357a0
https://doi.org/10.1002/ceat.270190512
https://doi.org/10.1002/ceat.270190512
Publikováno v:
The Chemical Engineering Journal and the Biochemical Engineering Journal. 63:181-188
Experiments were performed in liquid—solid loop reactor with a loop length of 14.45 m and an inner diameter of 90 mm under high velocity conditions. The variations in pressure gradient along the downflow, upflow and bend sections of the loop were i
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::21d8d1ba77ef551092b7f76398d78536
https://doi.org/10.1016/s0923-0467(96)03098-9
https://doi.org/10.1016/s0923-0467(96)03098-9
Publikováno v:
Zeolites. 17:297-303
The alkylation of benzene with dodecene over HY zeolite is studied in a stirred batch reactor. A special feature of the effect of the benzene to dodecene ratio on the reaction conversion is found. Even a low water content (0.04%) in the reactants gre
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::6d0aee0efb39b101e9371c9c36c72bf2
https://doi.org/10.1016/0144-2449(96)00034-6
https://doi.org/10.1016/0144-2449(96)00034-6
Publikováno v:
Chemical Engineering Science. 51:2001-2010
Electrical conductivity probes were used to measure the radial distributions of solids holdup and liquid velocity in a liquid-solid circulating fluidized bed. These distributions are found to be non-uniform, unlike those in a non-circulating bed. The
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::abc7729a6c290c047a5456d29a84f7da
https://doi.org/10.1016/0009-2509(96)00057-7
https://doi.org/10.1016/0009-2509(96)00057-7
Publikováno v:
The Canadian Journal of Chemical Engineering. 73:656-661
The hydrodynamics of a gas-liquid-solid circulating fluidized bed was investigated. A new regime, the three phase circulating fluidization regime, was discovered for the first time. The characteristics of this regime were compared with that of the co
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::126509602a40576e7ab441c1270f6a61
https://doi.org/10.1002/cjce.5450730509
https://doi.org/10.1002/cjce.5450730509