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The developments of syngas technologies are summarized in Section 1.
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Furthermore, an analysis of local sensitivity coefficients was carried out to determine the influence of selected reactions at the given experimental conditions and to identify those reactions that require more attention in future development of syngas combustion models.
While commercial development of syngas fermentation technology is underway, an unmet need is the development of integrated metabolic and transport models for industrially relevant syngas bubble column reactors.
In this paper we first undertake a brief overview of the catalyst development for syngas conversion to C2 oxygenates over Rh-based catalysts, mainly on the effects of various additives and supports on the activity and selectivity.
By contrast, growth in minimal medium in the presence of syngas was much slower, requiring ∼240 h (Figure 1).
Our results increase our understanding of O. carboxidovorans metabolism during heterotrophic and autotrophic growth and in particular provide information on proteomic changes during utilization of syngas for bioenergy.
The rate of production of syngas increased accordingly.
Volume of syngas produced per minute (cubic meters/min). .
The influence of gasifier temperature on syngas composition, gasifier efficiency, and LHV of syngas is illustrated in Figures10 and11.
This increases the raw syngas flow and the oxygen consumption, thus reducing the efficiency of syngas generation.
The relationships among syngas composition, reaction temperature, lower heating value of syngas and O2 content are shown in Fig. 3.
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