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Molten Salt Nio Oxygen Carrier Partial Oxidation Of Methane To Syngas In The Pilot Study

Posted on:2008-07-09Degree:MasterType:Thesis
Country:ChinaCandidate:C Y ZhangFull Text:PDF
GTID:2191360212486521Subject:Thermal Engineering
Abstract/Summary:PDF Full Text Request
The reaction of partial oxidation of methane(POM) to syngas before producing fuel and other chemical products has been one of the most promising natural gas utilization approaches. Currently, the synthesis gas is typically prepared through three routes: steam reforming with methane, POM and methane catalytic reforming with carbon dioxide. The ecommercialization of steam reforming has occurred. But there are some disadvantages: it will lead to large H2/CO ratio, and need high energy consumption. POM in catalyst bed can avoid these disadvantages, but this way needs produce pure oxygen before reaction and it will lead to hot-spot in catalyst bed for it is exothermic reaction and the mixture of CH4 and O2 is explosive gas, which are danger for large industrial scale. POM to syngas by lattice oxygen in molten salt medium system is introduced for utilizing reaction heat and avoiding hot spots and explosion in catalyst bed.The principle and mechanism have been studied by TG, DAT, TPD and TPR. The results showed that the molten salt medium system of wt% of Na2CO3-K2CO3 being 1 to 1 is suitable for this technique, and the best reaction temperature is about 800°C. It is suggested that reactions of POM to syngas using oxygen carriers of NiO, CeO2, Co3O4 and ZnO need different conditions by thermodynamics analysis. The NiO is responsible for POM in molten salts at 800°C.Conclusions of POM in catalyst bed: pure NiO as oxygen carrier, it can loss lattice oxygen to be Ni and the lattice oxygen can react with methane to syngas, carbon deposition and agglomeration were observed by SEM and TG analyses. The NiO oxygen carrier was prepared mixed with supports such as Al2O3 , MgO and SiO2. It was found that the NiO/Al2O3 oxygen carrier among those investigated always possess better POM performances, giving higher conversion of CH4 and higher selectivity for CO and H2, and lower CO2 and coke formations. NiO/NiAl2O4 oxygen carrier prepared by coprecipitation method showed the best cycle performance. It showed that NiO/NiAl2O4 would renew lattice oxygen about 100%,methane conversion, H2and CO selectivity were kept at 99.78%, 60% and 58.21% respectively.Conclusions of POM in molten salt: SEM-EDS analysis showed that NiOoxygen carrier distributed in molten salts unevenly. The added oxygen carrier and supports would affect stability of molten salts. Obvious interstice occurred in the middle of the molten salts by leading Methane. NiO oxygen carrier would lose lattice oxygen obviously. Substance composed of different quantities of elements would show different configuration. Aagglomeration was not observed in molten salts. After reacted with CH4, Oxygen carrier NiO/Al2O3 would renew lattice oxygen by reacting with oxygen in air. Methane would react with lattice oxygen firstly. Decomposition of methane would be the primary reaction when lack of lattice oxygen. Carbon deposition would affect the stability of molten salts too. The best condition of experiment is wt% of NiO/ (NiO + Al2O3) being 10% and flux of methane being 10ml/min at 800°C. The volume content of H2, CO and CO2 were kept at 63.4%, 30.25% and 6.35% respectively.In conclusion, POM to Syngas by Lattice of oxygen carriers in molten salt is a feasible and outstanding technology. NiO is appropriate for POM to syngas by Lattice of oxygen carriers in Molten Salt of wt% of Na2CO3 and K2CO3 being 1 to 1.
Keywords/Search Tags:molten salt, lattice oxygen, NiO, methane, partial oxidation, syngas
PDF Full Text Request
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