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CO2 Utilization-Co Based Catalysts Used For CO2 Methanation

Posted on:2019-06-24Degree:MasterType:Thesis
Country:ChinaCandidate:H R LiuFull Text:PDF
GTID:2321330548959554Subject:Environmental Engineering
Abstract/Summary:PDF Full Text Request
The sharp increase of CO2 concentration in atmosphere,caused by the intensive use of fossil fuels,leads to the serious global energy shortage and environmental problems.Thus,the chemical transformation and utilization of CO2 have received more attentions.CO2 methanation technology?Sabatier Reaction?,as an effective chemiacl method for CO2 utilization,can directly catalytic conversion of CO2 to chemicals and fuels CH4,and then the transformation of inorganic carbon to organic carbon is achieved.CO2 methanation technology can not only effectively reduce the concentration of CO2 in the atmosphere,but also promote the recycling of carbon resources.As the core of CO2 methanation technology,the catalyst has attracted the attention of the researchers.In this paper,the Co/KIT-6 catalysts were prepared by impregnation method.The physicochemical properties of the Co based catalysts were characterized by Scanning electronmicroscopy?SEM?,Transmissionelectronmicroscopy?TEM?,Brunauer-Emmett-Teller?BET?,hydrogentemperature-programmedreduction?H2-TPR?,X-ray diffraction?XRD?,X-ray photoelectron spectroscopy?XPS?,H2-temperature programmed desorption?H2-TPD?and CO2-temperature programmed desorption?CO2-TPD?.The effects of Co loading,reduction temperature,and crystallization temperature used for preparing mesoporous SiO2 support on the catalytic performance of the Co based catalysts were investigated.And some main conclusions were drawn as follows:1.The crystal size of Co species in Co/KIT-6 catalysts prepared by impregnation method increases with the increasing Co content and the dispersion of Co species reveals an opposite trend.The adsorption capacities of H2 and/or CO2 molecules achieve a maximum value at the Co loading of 25 wt%.The CO2 reaction rate and CH4selectivity are in the following order:Co15<Co20<Co30<Co25.With the increasing of Co loading,the CO2 reaction rate increases from 2.21×10-55 mol/gcat/s?CO2conversion of 29.8%?for the Co15 catalyst to 3.91×10-55 mol/gcat/s?CO2 conversion of52.6%?for the Co25 catalyst,and the CH4 selectivity improves from 67.0%for the Co15 catalyst to 94.5%for the Co25 catalyst at 360oC,while the other product is CO.The catalytic performance and products distribution of the Co/KIT-6 catalysts for CO2hydrogenation are sensitive to the crystal size of Co species which can be adjusted by changing the Co content in Co/KIT-6 catalysts.2.Reduction temperature has a significant impact on the specific surface area,crystallinity and content of Co0 species,and CO2 adsorption performance of the prepared Co/KIT-6 catalysts.The low reduction temperature is not conduct to the reduction of CoOx,while the high reduction temperature lead to the increase of Co0species crystallinity and the formation of Co2SiO4 and/or Co-O-Si species which are unfavorable to the form Co0species.The RT400 catalyst exhibits the highest Co0species content and the best CO2 adsorption performance.Both the CO2 hydrogenation catalytic activity and CH4 selectivity of the Co/KIT-6 catalysts follow the order:RT400>RT350>RT450>RT500>RT550,with a small amount of by-product CO.At the reaction temperature of 340oC,the CO2 reaction rate of the RT400 catalyst can reach2.98×10-55 mol/gcat/s?CO2 conversion of 40%?,the CH4 and CO selectivity are 86.7%and 13.3%,respectively.3.The pore size,specific surface area,and the Co0 species crystallinity of the Co/Si O2 catalyst prepared by grind-impregnation method increase with increasing crystallization temperature of preparing SiO2 support.The mesoporous Co/SiO2 catalyst has the best CO2 adsorption property when SiO2 support is prepared at the crystallization temperature of 100oC.The CO2 reaction rate?CO2 conversion?of the Co/Si O2 catalysts is as follows:CK100>CK080>CK120>CK060>CK140>CK040,and the CH4 selectivity follows the order:CK100>CK080>CK120>CK140>CK060>CK040,accompanied by a certain amount of by-product CO molecules.At 360oC,the CO2 reaction rate of the CK100 catalyst is up to 3.29×10-5mol/gcat/s?CO2 conversion of 44.3%?,the CH4 and CO selectivity are 86.5%and 13.5%,respectively.
Keywords/Search Tags:mesoporous Co/SiO2 catalyst, catalytic hydrogenation, CO2 methanation, metal Co loading, structure
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