The catalyst screening tests for carbon dioxide oxidative coupling of methane (CO2-OCM) have been investigated over ternary and binary metal oxide catalysts. The catalysts are prepared by doping MgO- and CeO2-based so...The catalyst screening tests for carbon dioxide oxidative coupling of methane (CO2-OCM) have been investigated over ternary and binary metal oxide catalysts. The catalysts are prepared by doping MgO- and CeO2-based solids with oxides from alkali (Li2O), alkaline earth (CaO), and transition metal groups (WO3 or MnO). The presence of the peroxide (O2-2) active sites on the Li2O2, revealed by Raman spectroscopy, may be the key factor in the enhanced performance of some of the Li2O/MgO catalysts. The high reducibility of the CeO2 catalyst, an important factor in the CO2-OCM catalyst activity, may be enhanced by the presence of manganese oxide species. The manganese oxide species increases oxygen mobility and oxygen vacancies in the CeO2 catalyst. Raman and Fourier Transform Infra Red (FT-IR) spectroscopies revealed the presence of lattice vibrations of metal-oxygen bondings and active sites in which the peaks corresponding to the bulk crystalline structures of Li2O, CaO, WO3 and MnO are detected. The performance of 5%MnO/15%CaO/CeO2 catalyst is the most potential among the CeO2-based catalysts, although lower than the 2%Li2O/MgO catalyst. The 2%Li2O/MgO catalyst showed the most promising C2+ hydrocarbons selectivity and yield at 98.0% and 5.7%, respectively.展开更多
Glycerol dehydration to acrolein over a series of supported silicotungstic acid catalysts(SiWx‐Al/Zry)was investigated.Characterization results showed that the final catalyst had high thermal stability,a large pore d...Glycerol dehydration to acrolein over a series of supported silicotungstic acid catalysts(SiWx‐Al/Zry)was investigated.Characterization results showed that the final catalyst had high thermal stability,a large pore diameter,strong Lewis acidic sites,and a large specific surface area.X‐ray photoelectron survey spectra clearly showed peaks attributable to W(W4f=35.8eV),Al2O3(Al2p=74.9eV),and ZrO2(Zr3d=182.8eV).The highest acrolein selectivity achieved was87.3%at97%glycerol conversion over the SiW20‐Al/Zr10catalyst.The prepared catalysts were highly active and selective for acrolein formation even after40h because of the presence of high concentrations of Lewis acidic sites,which significantly reduced the amount of coke on the catalyst surface.Response surface methodology optimization showed that87.7%acrolein selectivity at97.0%glycerol conversion could be obtained under the following optimal reaction conditions:0.5wt%catalyst,reaction temperature300°C,and feed glycerol concentration10wt%.Evaluation of a mass‐transfer‐limited regime showed the absence of internal and external diffusions over pellets of diameter dP<20μm.These results show that glycerol dehydration over a strong Lewis acid catalyst is a promising method for acrolein production.展开更多
This paper deals with thermodynamic chemical equilibrium analysis using the method of direct minimization of Gibbs free energy for all possible CH4 and CO2 reactions. The effects of CO2/CH4 feed ratio, reaction temper...This paper deals with thermodynamic chemical equilibrium analysis using the method of direct minimization of Gibbs free energy for all possible CH4 and CO2 reactions. The effects of CO2/CH4 feed ratio, reaction temperature, and system pressure on equilibrium composition, conversion, selectivity and yield were studied. In addition, carbon and no carbon formation regions were also considered at various reaction temperatures and CO2/CH4 feed ratios in the reaction system at equilibrium. It was found that the reaction temperature above 1100 K and CO2/CH4 ratio=1 were favourable for synthesis gas production with H2/CO ratio unity, while carbon dioxide oxidative coupling of methane （CO2 OCM） reaction to produce ethane and ethylene is less favourable thermodynamically. Numerical results indicated that the no carbon formation region was at temperatures above 1000 K and CO2/CH4 ratio larger than 1.展开更多
A dual-bed catalytic system is proposed for the direct conversion of methane to liquid hydrocarbons. In this system, methane is converted in the first stage to oxidative coupling of methane （OCM） products by selecti...A dual-bed catalytic system is proposed for the direct conversion of methane to liquid hydrocarbons. In this system, methane is converted in the first stage to oxidative coupling of methane （OCM） products by selective catalytic oxidation with oxygen over La-supported MgO catalyst. The second bed, comprising of the HZSM-5 zeolite catalyst, is used for the oligomerization of OCM light hydrocarbon products to liquid hydrocarbons. The effects of temperature （650-800 ℃）, methane to oxygen ratio （4-10）, and SIO2/Al2O3 ratio of the HZSM-5 zeolite catalyst on the process are studied. At higher reaction temperatures, there is considerable dealumination of HZSM-5, and thus its catalytic performance is reduced. The acidity of HZSM-5 in the second bed is responsible for the oligomerization reaction that leads to the formation of liquid hydrocarbons. The activities of the oligomerization sites were unequivocally affected by the SiO2/Al2O3 ratio. The relation between the acidity and the activity of HZSM-5 is studied by means of TPD-NH3 techniques. The rise in oxygen concentration is not beneficial for the C5＋ selectivity, where the combustion reaction of intermediate hydrocarbon products that leads to the formation of carbon oxide （CO＋CO2） products is more dominant than the oligomerization reaction. The dual-bed catalytic system is highly potential for directly converting methane to liquid fuels.展开更多
Background:A key step in gene expression is the recognition of the stop codon to terminate translation at the correct position.However,it has been observed that ribosomes can misinterpret the stop codon and continue t...Background:A key step in gene expression is the recognition of the stop codon to terminate translation at the correct position.However,it has been observed that ribosomes can misinterpret the stop codon and continue the translation in the 3′UTR region.This phenomenon is called stop codon read-through(SCR).It has been suggested that these events would occur on a programmed basis,but the underlying mechanisms are still not well understood.Methods:Here,we present a strategy for the comprehensive identification of SCR events in the Drosophila melanogaster transcriptome by evaluating the ribosomal density profiles.The associated ribosomal leak rate was estimated for every event identified.A statistical characterization of the frequency of nucleotide use in the proximal region to the stop codon in the sequences associated to SCR events was performed.Results:The results show that the nucleotide usage pattern in transcripts with the UGA codon is different from the pattern for those transcripts ending in the UAA codon,suggesting the existence of at least two mechanisms that could alter the translational termination process.Furthermore,a linear regression models for each of the three stop codons was developed,and we show that the models using the nucleotides at informative positions outperforms those models that consider the entire sequence context to the stop codon.Conclusions:We report that distal nucleotides can affect the SCR rate in a stop-codon dependent manner.展开更多
文摘The catalyst screening tests for carbon dioxide oxidative coupling of methane (CO2-OCM) have been investigated over ternary and binary metal oxide catalysts. The catalysts are prepared by doping MgO- and CeO2-based solids with oxides from alkali (Li2O), alkaline earth (CaO), and transition metal groups (WO3 or MnO). The presence of the peroxide (O2-2) active sites on the Li2O2, revealed by Raman spectroscopy, may be the key factor in the enhanced performance of some of the Li2O/MgO catalysts. The high reducibility of the CeO2 catalyst, an important factor in the CO2-OCM catalyst activity, may be enhanced by the presence of manganese oxide species. The manganese oxide species increases oxygen mobility and oxygen vacancies in the CeO2 catalyst. Raman and Fourier Transform Infra Red (FT-IR) spectroscopies revealed the presence of lattice vibrations of metal-oxygen bondings and active sites in which the peaks corresponding to the bulk crystalline structures of Li2O, CaO, WO3 and MnO are detected. The performance of 5%MnO/15%CaO/CeO2 catalyst is the most potential among the CeO2-based catalysts, although lower than the 2%Li2O/MgO catalyst. The 2%Li2O/MgO catalyst showed the most promising C2+ hydrocarbons selectivity and yield at 98.0% and 5.7%, respectively.
基金the Ministry of Science, Technology and Innovation (MOSTI), Malaysia for supporting the project under project no. 03–01–06–SF0963
文摘Glycerol dehydration to acrolein over a series of supported silicotungstic acid catalysts(SiWx‐Al/Zry)was investigated.Characterization results showed that the final catalyst had high thermal stability,a large pore diameter,strong Lewis acidic sites,and a large specific surface area.X‐ray photoelectron survey spectra clearly showed peaks attributable to W(W4f=35.8eV),Al2O3(Al2p=74.9eV),and ZrO2(Zr3d=182.8eV).The highest acrolein selectivity achieved was87.3%at97%glycerol conversion over the SiW20‐Al/Zr10catalyst.The prepared catalysts were highly active and selective for acrolein formation even after40h because of the presence of high concentrations of Lewis acidic sites,which significantly reduced the amount of coke on the catalyst surface.Response surface methodology optimization showed that87.7%acrolein selectivity at97.0%glycerol conversion could be obtained under the following optimal reaction conditions:0.5wt%catalyst,reaction temperature300°C,and feed glycerol concentration10wt%.Evaluation of a mass‐transfer‐limited regime showed the absence of internal and external diffusions over pellets of diameter dP<20μm.These results show that glycerol dehydration over a strong Lewis acid catalyst is a promising method for acrolein production.
文摘This paper deals with thermodynamic chemical equilibrium analysis using the method of direct minimization of Gibbs free energy for all possible CH4 and CO2 reactions. The effects of CO2/CH4 feed ratio, reaction temperature, and system pressure on equilibrium composition, conversion, selectivity and yield were studied. In addition, carbon and no carbon formation regions were also considered at various reaction temperatures and CO2/CH4 feed ratios in the reaction system at equilibrium. It was found that the reaction temperature above 1100 K and CO2/CH4 ratio=1 were favourable for synthesis gas production with H2/CO ratio unity, while carbon dioxide oxidative coupling of methane （CO2 OCM） reaction to produce ethane and ethylene is less favourable thermodynamically. Numerical results indicated that the no carbon formation region was at temperatures above 1000 K and CO2/CH4 ratio larger than 1.
文摘A dual-bed catalytic system is proposed for the direct conversion of methane to liquid hydrocarbons. In this system, methane is converted in the first stage to oxidative coupling of methane （OCM） products by selective catalytic oxidation with oxygen over La-supported MgO catalyst. The second bed, comprising of the HZSM-5 zeolite catalyst, is used for the oligomerization of OCM light hydrocarbon products to liquid hydrocarbons. The effects of temperature （650-800 ℃）, methane to oxygen ratio （4-10）, and SIO2/Al2O3 ratio of the HZSM-5 zeolite catalyst on the process are studied. At higher reaction temperatures, there is considerable dealumination of HZSM-5, and thus its catalytic performance is reduced. The acidity of HZSM-5 in the second bed is responsible for the oligomerization reaction that leads to the formation of liquid hydrocarbons. The activities of the oligomerization sites were unequivocally affected by the SiO2/Al2O3 ratio. The relation between the acidity and the activity of HZSM-5 is studied by means of TPD-NH3 techniques. The rise in oxygen concentration is not beneficial for the C5＋ selectivity, where the combustion reaction of intermediate hydrocarbon products that leads to the formation of carbon oxide （CO＋CO2） products is more dominant than the oligomerization reaction. The dual-bed catalytic system is highly potential for directly converting methane to liquid fuels.
基金LIE is funded by CONICET Ph.D.Fellowship.AMA and LD are researchers of CONICET(Argentina).JRR is Full Professor at the UNLP(Argentina).This work was supported by CONICET,Argentina(PIP2017-00059).
文摘Background:A key step in gene expression is the recognition of the stop codon to terminate translation at the correct position.However,it has been observed that ribosomes can misinterpret the stop codon and continue the translation in the 3′UTR region.This phenomenon is called stop codon read-through(SCR).It has been suggested that these events would occur on a programmed basis,but the underlying mechanisms are still not well understood.Methods:Here,we present a strategy for the comprehensive identification of SCR events in the Drosophila melanogaster transcriptome by evaluating the ribosomal density profiles.The associated ribosomal leak rate was estimated for every event identified.A statistical characterization of the frequency of nucleotide use in the proximal region to the stop codon in the sequences associated to SCR events was performed.Results:The results show that the nucleotide usage pattern in transcripts with the UGA codon is different from the pattern for those transcripts ending in the UAA codon,suggesting the existence of at least two mechanisms that could alter the translational termination process.Furthermore,a linear regression models for each of the three stop codons was developed,and we show that the models using the nucleotides at informative positions outperforms those models that consider the entire sequence context to the stop codon.Conclusions:We report that distal nucleotides can affect the SCR rate in a stop-codon dependent manner.
