@article { ISI:000277822200012, title = {Thermodynamic analysis of dry autothermal reforming of glycerol}, journal = {Fuel Processing Technology}, volume = {91}, number = {5}, year = {2010}, month = {MAY}, pages = {520-530}, publisher = {ELSEVIER SCIENCE BV}, address = {PO BOX 211, 1000 AE AMSTERDAM, NETHERLANDS}, abstract = {

{Dry autothermal reforming of glycerol uses a combination of dry (CO(2)) reforming and partial oxidation reactions to produce syngas rich product stream. Thermodynamic equilibrium data for dry autothermal reforming of glycerol was generated for temperature range 600-1000 K . 1 bar pressure, OCGR [feed O(2)/C (C of glycerol only) ratio] 0.1 to 0.5 and CGR [feed CO(2)/glycerol ratio] 1 to 5 and analyzed. The objective of the paper is to identify the thermodynamic domain of the process operation, study the variation of product distribution pattern and describe the optimum conditions to maximize yield of the desired product and minimize the undesired product formation. Higher OCGR and higher CGR yielded a syngas ratio (similar to 1), with lower carbon and methane formation, while lower CGR and lower OCGR yielded good hydrogen and total hydrogen, with low water and CO2 production. The best thermoneutral condition for DATR of glycerol operation was seen at a temperature of 926.31 K at 1 bar pressure

}, keywords = {CO(2) reforming, Dry reforming, Glycerol reforming, Syngas production, Thermodynamic modeling}, issn = {0378-3820}, doi = {10.1016/j.fuproc.2009.12.015}, author = {Kale, Ganesh R. and Kulkarni, Bhaskar D.} } @article { ISI:000309370500015, title = {Carbon dioxide reforming of methane over ruthenium substituted strontium titanate perovskite catalysts}, journal = {Indian Journal of Chemistry Section A-Inorganic Bio-Inorganic Physical Theoretical \& Analytical Chemistry}, volume = {51}, number = {9-10, SI}, year = {2012}, month = {SEP}, pages = {1339-1347}, publisher = {NATL INST SCIENCE COMMUNICATION-NISCAIR}, address = {DR K S KRISHNAN MARG, PUSA CAMPUS, NEW DELHI 110 012, INDIA}, abstract = {

Strontium titanate (SrTiO3) doped with varying amounts of ruthenium (7.9, 15.6 and 31 wt\%) have been prepared by the citrate gel synthesis method. Structural and textural characterizations reveal that at lower concentrations, a major part of Ru is incorporated in the lattice of SiTiO3. The content of surface Ru (outside lattice) increases with increasing amounts of the doped Ru. The surface Ru reduced at lower temperatures compared to Ru incorporated into the lattice. The reduction of the lattice substituted Ru occurs only at temperatures above the collapse of the perovskite structure. The catalyst sample with 7.9 wt\% of Ru shows good conversions in the dry reforming of methane with CO2. The conversion of CO2 is in excess compared to methane under the studied reaction conditions. As a result, H-2/CO ratio of the product gases which should have been equivalent to unity is lower than the stoichiometric value. This ratio is particularly low when lower reaction temperatures (873-973 K) were used. Similar was the case when high space velocities were used. Low methane conversion and reverse water gas shift reaction are the causes for the low H-2/CO ratios.

}, keywords = {Carbon dioxide reforming, Catalysts, Citrate gel method, Doped catalysts, Dry reforming, Methane reforming, Perovskites, Reverse water gas shift, Ruthenium doped catalysts, Strontium titanate, Syngas}, issn = {0376-4710}, author = {Gurav, Hanmant R. and Bobade, Richa and Das, Vineetha Lakshmi and Chilukuri, Satyanarayana V.} } @article { ISI:000334984000005, title = {Methane reforming with carbon dioxide over La-Ni-x-Ce1-x mixed oxide catalysts}, journal = {Indian Journal of Chemistry Section A-Inorganic Bio-Inorganic Physical Theoretical \& Analytical Chemistry}, volume = {53}, number = {4-5, SI}, year = {2014}, month = {FEB}, pages = {478-483}, publisher = {NATL INST SCIENCE COMMUNICATION-NISCAIR}, address = {DR K S KRISHNAN MARG, PUSA CAMPUS, NEW DELHI 110 012, INDIA}, abstract = {

La-Ni-x-Ce1-x mixed oxide (0 \<= x \<= 1) catalysts have been hydrothermally prepared, characterized by physico-chemical techniques and evaluated for CO2 reforming of methane. High conversions are achieved for both methane and carbon dioxide over the LaNi0.6Ce0.4O3 catalyst tested under the conditions of CO2/CH4/N-2 ratio of 80/80/80. (total flow rate = 240 mL/min), space velocity of 28,800 h(-1) and at a temperature of 800 degrees C. The H-2/CO ratio in the syngas is stable at 0.93 +/- 0.02. Exchanging Ni with Ce, rather than with La as reported in the literature, appears to be a better option for the improved performance of the catalysts.

}, keywords = {Carbon dioxide reforming, Catalysts, Cerium, Dry reforming, Hydrothermal synthesis, Lanthanum, Methane reforming, Mixed oxides, Nickel}, issn = {0376-4710}, author = {Sagar, T. V. and Sreelatha, N. and Hanmant, G. and Upendar, K. and Lingaiah, N. and Rao, Kamaraju Seetha Rama and Satyanarayana, C. V. V. and Reddy, I. A. K. and Prasad, P. S. Sai} } @article { ISI:000334306500004, title = {Thermoneutral conditions in dry reforming of ethanol}, journal = {Asia-Pacific Journal of Chemical Engineering}, volume = {9}, number = {2}, year = {2014}, month = {MAR}, pages = {196-204}, publisher = {WILEY-BLACKWELL}, address = {111 RIVER ST, HOBOKEN 07030-5774, NJ USA}, abstract = {

The reaction enthalpy (Delta H) of reforming processes like steam and dry (CO2) reforming is of great importance for scale-up and process development. Generally, the reforming processes are considered endothermic in nature. However, a detailed study of the reaction enthalpy of reforming process, taking the example of dry reforming of ethanol considered in this study, reveals the existence of exothermic reaction enthalpy at low temperatures. A study of reaction enthalpy of ethanol dry reforming within pressure (1-10 bar), temperature range (300-900 degrees C), and CO2 to carbon in ethanol ratio (CCER 1-5) was initiated to determine the existence of thermoneutral temperatures for the overall reaction. The variation of thermoneutral conditions and product yields at the thermoneutral temperatures was studied. The utilization potential of the products generated at thermoneutral conditions was also evaluated. The low-pressure thermoneutral operation favored higher hydrogen production, lower methane and water formation, whereas the high-pressure thermoneutral operation favored product gas of lower syngas ratio with higher CO2 conversion (utilization) in the process. The study can be extended to steam and dry reforming of other fuels to generate valuable products at thermoneutral conditions avoiding use of air in the process and subsequent N-2 dilution of the product gas. (c) 2013 Curtin University of Technology and John Wiley \& Sons, Ltd.

}, keywords = {carbon nanofilaments, CO2 utilization, Dry reforming, ethanol to syngas, thermoneutral process}, issn = {1932-2135}, doi = {10.1002/apj.1759}, author = {Kale, Ganesh R. and Kulkarni, Bhaskar D.} } @article {44447, title = {Tuning the dimensionality of layered Srn+1Tin-xNixO3n+1 perovskite structures for improved activity in syngas generation}, journal = {Journal of Catalysis}, volume = {360}, year = {2018}, month = {APR }, pages = {27-39}, type = {Journal Article}, abstract = {

Interest in perovskite type oxides is growing due to their versatile catalytic applications. A series of Ruddlesden-Popper (RP) type layered perovskite oxides Srn+1Tin-xNixO3n+1 were prepared and evaluated for their catalytic activity in steam reforming, CO2 reforming and bi-reforming of methane. These materials, prepared through citrate gel method were characterized to understand their structure and Ni reducibility. Substitution of Ni in RP phases was established through refinement of XRD powder pattern. During methane reforming, the catalytic activity increased with the order of RP phase of SrTi1-xNixO3-δ (n = $\infty$). TPR results show variation in Ni reducibility with the order of RP phase, while TPD-O2 study helped to estimate oxygen vacancies. These vacancies seem to influence catalytic activity during methane reforming. Transient pulse experiments show that CO2 dissociates over oxygen vacancies to give CO and oxygen, with later replenishing lattice oxygen in SrTi0.8Ni0.2O3-δ (n = $\infty$) phases. Highly labile oxygen vacancies generated in the bulk of SrTi0.8Ni0.2O3-δ must be migrating to the surface, helping in the removal of coke formed. Characterization of catalysts after reaction helped in better understanding of coke precursors.

}, keywords = {Dry reforming, NickelSyngas, Ruddlesden-Popper (RP) perovskites, Steam reforming}, issn = {219517}, doi = {10.1016/j.jcat.2018.01.015}, author = {Dama, Srikanth}, editor = {Ghodke, Seema} } @article {46145, title = {Dry reforming of methane in DBD plasma over Ni-based catalysts: influence of process conditions and support on performance and durability}, journal = {Energy Technology}, volume = {7}, year = {2019}, month = {APR}, pages = {1801008}, type = {Article}, abstract = {

The conversion of greenhouse gases, H-2 and CO selectivity, H-2/CO ratio, and carbon formation in the dry reforming reaction over Ni-supported ZSM-5, Al2O3, and TiO2 are tested under thermal, plasma, and plasma-thermal conditions. It is observed that the dielectric nature, specific surface area, and acid-base properties of the support influence the performance during the DRM reaction. Typical results indicate that the best activity and syngas yield are achieved with 15Ni/Al2O3 under plasma conditions, possibly due to the high dielectric constant and surface area of Al2O3 and nanosize of Ni. In the thermal condition, the highest conversion of 73\% and 68\% for CH4 and CO2, respectively, is achieved over 15Ni/ZSM-5 at 500 degrees C. Plasma-assisted thermal conditions provide the highest conversion due to the activation of reactants and their partial conversion in the plasma zone before entering into the catalytic zone. The plasma-assisted thermocatalytic conversions of CH4 and CO2 reach the best values of 76\% and 71\%, respectively, on 15Ni/ZSM-5. Under the same conditions, 68\% and 65\% conversion of CH4 and CO2, respectively, is achieved with 15Ni/Al2O3 where the selectivity for H-2 and CO is 45\% and 58\%, respectively.

}, keywords = {DBD plasma, Dry reforming, reaction conditions, supported catalysts, Syngas}, issn = {2194-4288}, doi = {10.1002/ente.201801008}, author = {Ray, Debjyoti and Nepak, Devadutta and Janampelli, Sagar and Goshal, Partha and Subrahmanyam, Ch} }