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The conversion started immediately with a high rate.
If the amount of benzenesulfonic acid continued to rise, the increase of the conversion started to be slow.
Our detailed IR investigation allowed the identification of the active sites and the adsorbed species and demonstrated that the conversion started from 350 °C with alkoxy group as the intermediate.
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In fact, the conversion starts at a temperature of about 600 °C, and finishes at 850 °C with a loss of 44 wt % corresponding to the stoichiometric CO2 amount in CaCO3 (Rodriguez-Navarro et al. 2009).
The presence of transients shifted the conversion starts of CO and propene as well as their light-off temperatures towards lower temperatures.
After the design phase, hospitals completed the conversion (start of construction to patient acceptance) on an average of 13 days, resulting in a total of 698 negative-pressure AIIRs constructed by the completion of the nationwide project.
With a simulated reformate mixture (5% CO + 20% H2O + 11% CO2 + 40% H2, N2 balance), the equilibrium WGS curve was exceeded for both catalysts (for the HT-prepared catalyst, CO conversion started at lower temperature and reached 100%), due to the parasite methanation reactions of both CO and CO2, favoured by the presence of a large hydrogen concentration in the reactor.
The screening at powder level in a fixed bed micro-reactor highlighted that feeding 5% CO and 20% H2O (N2 balance) with the HT-prepared catalyst, CO conversion started at slightly lower temperature, but CH4 outlet concentrations were higher than those of the SCS-prepared one.
The inferred boundaries for gene conversion started between nucleotide 1284 and 1306, which are within 25 bp downstream of the nucleotide position 1281 that was inferred by visual inspection of the protein sequences.
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CEO of Professional Science Editing for Scientists @ prosciediting.com