scholarly journals Optimum operating conditions of vinyl acetate synthesis from acetylene by fluidized-bed reactor.

1986 ◽  
Vol 12 (6) ◽  
pp. 627-634 ◽  
Author(s):  
Toshio Kawaguchi ◽  
Toshihisa Wakasugi
2018 ◽  
Vol 169 ◽  
pp. 207-216 ◽  
Author(s):  
Carolina Montero ◽  
Aingeru Remiro ◽  
Pedro Luis Benito ◽  
Javier Bilbao ◽  
Ana G. Gayubo

2012 ◽  
Vol 518-523 ◽  
pp. 3483-3487
Author(s):  
Wen Wen Qu ◽  
Wen Jin ◽  
Jin Hui Peng ◽  
Shu Yang

ZnO/AC composite was prepared from spent catalyst of vinyl acetate synthesis by using conventional thermal treatment under CO2 atmosphere. The final composite was obtained with the operating conditions of activation temperature of 950°C, activation time of 120min and the CO2 flow rate of 600ml/min. The structure and surface properties of the ZnO/AC composite were observed and characterized by scanning electron microscope (SEM-EDX), X-ray diffraction (XRD), fourier transform infrared spectroscopy (FT-IR) and the UV diffuse reflectance spectra. It was found that the zinc acetate present in the spent catalyst is transformed to zinc oxide (ZnO) after thermal treatment. ZnO particles were well adhered and uniformly distributed onto the carbon surface, forming ZnO/AC composite. The thermal treatment of the spent catalyst gives rise to a material with excellent adsorptive and photocatalytic properties.


2011 ◽  
Vol 5 (5) ◽  
pp. 1190-1198 ◽  
Author(s):  
Luis F. de Diego ◽  
Margarita de las Obras-Loscertales ◽  
Francisco García-Labiano ◽  
Aránzazu Rufas ◽  
Alberto Abad ◽  
...  

2013 ◽  
Vol 860-863 ◽  
pp. 450-455 ◽  
Author(s):  
Qian Liu ◽  
Bao Sheng Jin

For biomass gasification, the high tar and carbon monoxide contents and the low heat value of fuel gas are problems to be solved, which leading to the poor operating conditions of the completed projects in China. Therefore, a new technology of biomass oxygen-enriched gasification in pressurized fluidized bed is proposed. Coupling the technologies of pressurized biomass oxygen-enriched gasification at low temperature, high-temperature gasification and melting, steam reforming and hydrocarbon synthesis, the high gasification efficiency, tar cracking and gas reforming shall be realized, and the middle/high heat value gas which meets the national standards will be produced. ASPEN PLUS simulation was carried out for biomass oxygen-enriched gasification. Both the equivalent ratio and gas yield of rice husk are lower than that of the wood sawdust, while the gas calorific values are equivalent. Considering the gas yield, the calorific value and economy, the optimum operating conditions are obtained: the gasification temperature at 1200 °C, the oxygen purity at 0.9, the equivalent ratio at about 0.25, the S/B ratio at 0.1~0.2. The gas yield could reach 1.9 m3/kg, and the gas calorific value was above 11 MJ/m3.


2011 ◽  
Vol 236-238 ◽  
pp. 1537-1545
Author(s):  
Wen Jing Liu ◽  
Hui Zhao ◽  
Chao He Yang ◽  
Hong Hong Shan

In fixed-fluidized bed reactor, laboratory evaluation of different catalyst, raw materials and process parameters can be implemented, so it has wide applications in the refining process. In this study, we focused on small fixed-fluidized bed reactor, using Eulerian-Eulerian two-fluid model, simulated the gas-solid flow behavior in it. Gas residence time distribution was measured in order to characterize macro-mixing. At the same time, by changing the reactor structure and operating conditions, we studied their effects on gas-solid macro-mixing characterization. The results show that the effects of structural parameters are larger than operating conditions, and different parameters have different effects. Different parameters can be adjusted to change the gas-solid macro-mixing characterization in small fixed-fluidized bed reactor. Therefore, the small fixed-fluidized bed reactor can provide better results in more application areas.


2012 ◽  
Vol 586 ◽  
pp. 274-281
Author(s):  
Mohammad Kazemeini ◽  
Reza Maleki ◽  
Moslem Fattahi

The FT reaction involves the conversion of syngas which is derived from natural gas or coal to different kinds of products according to the operating conditions and the type of the catalyst. In other words, it is a practical way to convert solid fuel (coal) and natural gas to various hydrocarbons (C1-C60) and oxygenates such as alkanes, alkenes etc. The main products of the reaction are naphtha and gasoline. This paper deals with developing a proper product distribution model for FT process using the appropriate kinetic model, optimizing the respective rate constants while applying them in product distribution equations. The results revealed only 8.09% deviations from the olefin experimental data and 10.27% deviations from the paraffin experimental data being acceptable when compared with previous open literature data.


Author(s):  
Hassan Hashemipour ◽  
Saeid Baroutian ◽  
Esmail Jamshidi ◽  
Alireza Abazari

In this work, thermal activation of pistachio shell was studied in a fluidized bed reactor. The effects of operating conditions on the pore development within the char particles were studied experimentally. The results showed that activation temperature, residence time, oxidizing gas type and concentration have main effects on the Iodine adsorption capacity of the product. The highest surface area was obtained using steam activation at temperature 850°C for 45 min. The synthesis process was also simulated using artificial neural networks (ANNs) to estimate the Iodine number of the product. The present work applied a Tan-sigmoid transfer function in three layers in the feed forward neural network with back propagation algorithm. The results of the network are in good agreement with the experimental data with a maximum relative deviation of 0.015%.


2020 ◽  
Vol 59 (44) ◽  
pp. 19522-19530
Author(s):  
Mateus V. C. da Silva ◽  
Amanda B. S. Rangel ◽  
Leandro G. Aguiar ◽  
Heizir F. de Castro ◽  
Larissa de Freitas

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