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Preparation and Characterization of New Cobalt Based Catalyst for F-T Synthesis
Author: MiaoPeng
Tutor: XuZhenGang;WangNaiJi
School: CCRI
Course: Chemical processes
Keywords: F-T synthesis Slurry bed reactor Cobalt-based catalyst
CLC: TQ529.2
Type: Master's thesis
Year: 2008
Downloads: 246
Quote: 0
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Abstract
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Cobalt-based catalysts for FT synthesis the catalyst for one of the most promising because of its higher hydrogenation activity and lower water-gas shift activity. The activated alumina the ZrO 2 modified activated alumina carrier, cobalt nitrate, cobalt source preparation methods on the physical and chemical properties of the catalyst, and to study the catalyst in the slurry bed FT synthesis reaction Performance. The catalyst prepared by impregnation method, were characterized by XRD, SEM, TEM, TPR and other physical and chemical properties of the catalyst. This thesis work mainly includes the following aspects: (1) using the immersion method were used to the slow drying fast drying prepared by different cobalt content of Co / Al 2 O 3 < / sub> catalyst. Characterization: The results show that the nature of the different drying methods obtained in the FT synthesis catalyst with a relatively large difference. Cobalt species on the catalyst Co 3 O 4 in the form of stored memory. Slow drying of the catalyst prepared in the formation of oxide crystals larger particles, and the smaller average pore diameter. The catalyst prepared by the two methods are difficult to restore the species the Co. 2 AlO 4 , and the impact of the utilization of the metal cobalt. Derived from the the TPR curve and XRD spectra comparison results can be difficult to restore Co 2 the AlO 4 and AlO (OH) are more slow drying prepared catalyst contains. (2) preparing a ZrO 2 -modified alumina carrier, and the carrier structure, properties and carries a cobalt-based catalyst research. The results showed that, of ZrO 2 -modified alumina carrier in the Texture compared to the alumina has a certain difference. The use of ZrO 2 -modified alumina carrier, to a source for cobalt nitrate for drilling, using the dipping method, preparation of a slow drying process of the FT synthesis catalyst. The characterization results proved that the cobalt species in the catalyst is still based on Co 3 O 4 form of catalyst shape and grain size, there was no significant change. TPR curves can be apparent, to Cart of ZrO 2 the promoted catalysts difficult to restore Co 2 an AlO 4 , and AlO (OH) content greatly reduced. (3) in the slurry bed reactor build their own hexadecane as the solvent of the slurry phase FT synthesis catalyst performance evaluation. Selected one of the FT synthesis catalyst in a slurry bed reactor, the reaction temperature, pressure, space velocity of the raw material gas on the conversion rate of the raw material gas. Determine the best reaction process parameters: P = 2.0MPa, T = 500K, H 2 / CO = 2.0, airspeed = 500h -1 sup>. In the reaction under the reaction conditions on the catalyst plus additives and adding additives Characterization.
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