Activated aluminum oxide selectively retaining long chain n-alkanes. Part I, description of the retention properties

2009 ◽  
Vol 634 (1) ◽  
pp. 96-101 ◽  
Author(s):  
Katell Fiselier ◽  
Dennis Fiorini ◽  
Koni Grob
1978 ◽  
Vol 14 (8) ◽  
pp. 591-593
Author(s):  
N. P. Poezd ◽  
I. Ya. Perezhigina ◽  
E. D. Radchenko ◽  
D. F. Poezd ◽  
A. V. Agafonov ◽  
...  

Author(s):  
Alexander P. Savostyanov ◽  
Roman E. Yakovenko ◽  
Grigory B. Narochny ◽  
Vera G. Bakun ◽  
Alexander A. Merkin

The compositions, methods of preparation and specific technological parameters of the production processes of cobalt catalysts for the synthesis of long chain hydrocarbons from synthesis gas were justified. To obtain C35+ selective catalysts by coprecipitation of active components, the carrier must provide a polydisperse distribution of the pore volume along the radii. This is achieved by hydrothermal treatment of the aluminosilicate carrier. To increase the strength of catalysts, it is possible to incorporate natural bentonites and diatomite of Roctov region deposits into the composition of coprecipitated catalysts. Effective catalytic systems are impregnated catalysts on Al2O3 and SiO2 supports with aluminum oxide promotion. The insertion of 5% - Al2O3 of cobalt metal mass allows to form crystallites of Co-CoO system with a size of 8 nm on the SiO2 surface, which provides high activity and selectivity for ceresin. Aluminum oxide is stabilized with Co3O4 in a structure with a high degree of ordering, without hindering its reduction, with the formation of cobalt predominantly with the crystalline structure of hexagonal close packing. Catalyst technologies are implemented in industry. The catalysts underwent continuous continuous testing (1000 h) in laboratory and industrial conditions, showed high stability of operation. During the entire operation, the yield of C5+ hydrocarbons was 159-171 g/Nm3 based on the processed synthesis gas. The long-chain hydrocarbons C35+ (ceresin) obtained are of high quality: the dropping point was 114-116 °C (37-40% ceresin content). Operation during the year of two industrial reactors at the Novocherkassk plant of synthetic products with a total volume of catalyst loading of 18 m3 confirmed the results of laboratory tests. For citation: Savostyanov A.P., Yakovenko R.E., Narochny G.B., Bakun V.G., Merkin A.A. Development and industrial approbation of technologies of cobalt catalysts for synthesis of long chain hydrocarbons from synthesis gas. Izv. Vyssh. Uchebn. Zaved. Khim. Khim. Tekhnol. 2018. V. 61. N 9-10. P. 53-58


1980 ◽  
Vol 16 (4) ◽  
pp. 281-284
Author(s):  
N. P. Poezd ◽  
E. D. Radchenko ◽  
D. F. Poezd

2015 ◽  
Vol 07 (11) ◽  
pp. 843-850
Author(s):  
Junling Wang ◽  
Xueming Wang ◽  
Cuimin Feng ◽  
Sheng Wei

1986 ◽  
Vol 22 (10) ◽  
pp. 512-515
Author(s):  
V. F. Klaptsov ◽  
S. A. Surin ◽  
G. D. Chukin ◽  
B. K. Nefedov

2012 ◽  
Vol 476-478 ◽  
pp. 1965-1968
Author(s):  
Da Lei Zhang ◽  
Fan Qiao ◽  
Mou Lv ◽  
Ying Jie Sun ◽  
Qing Yuan Guo

In this paper the adsorption properties of activated aluminum oxide (AAO ) to As(V) were researched. The effect of operating factors such as pH, contact time and initial As(V) concentration was investigated and the optimum operating conditions were established. Experimental results indicated that the optimal pH value adsorption of As(V)by activated aluminum oxide was from 4 to 6, and the optimum initial pH values was 5.5.The adsorption equilibrium was achieved within 5h.The adsorption capacity for As(V)increased with increasing concentration and the adsorption date was well fit by the Langmuir isotherm model. It is believed that activated aluminum oxide (AAO) is environmentally acceptable and industrially application for utilization in arsenic-containing wastewater treatment.


2015 ◽  
Vol 269 ◽  
pp. 351-357 ◽  
Author(s):  
Jie Xie ◽  
Yan Lin ◽  
Chunjie Li ◽  
Deyi Wu ◽  
Hainan Kong

Sign in / Sign up

Export Citation Format

Share Document