2021
DOI: 10.3390/su13031061
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Empirical Design, Construction, and Experimental Test of a Small-Scale Bubbling Fluidized Bed Reactor

Abstract: The methods currently used for designing a fluidized bed reactor in gasification plants do not meet an integrated methodology that optimizes all the different parameters for its sizing and operational regime. In the case of small-scale (several tens of kWs biomass gasifiers), this design is especially complex, and, for this reason, they have usually been built in a very heuristic trial and error way. In this paper, an integrated methodology tailoring all the different parameters for the design and sizing of a … Show more

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Cited by 11 publications
(10 citation statements)
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“…To determine the air speed, we first find the Reynolds criterion and the Archimedes criterion using the criterion dependences of O.M. Todes [ 34 , 35 ].…”
Section: The Basic Part Of the Studymentioning
confidence: 99%
See 1 more Smart Citation
“…To determine the air speed, we first find the Reynolds criterion and the Archimedes criterion using the criterion dependences of O.M. Todes [ 34 , 35 ].…”
Section: The Basic Part Of the Studymentioning
confidence: 99%
“…The research method is based on an improved method for studying the process of freezing juicy food products, such as sliced vegetables, berries, or fruits [ 15 , 16 , 17 , 28 , 29 , 30 , 31 , 32 , 33 , 34 , 35 , 36 , 37 ]. Two-stage freezing was used with the formation of a frozen layer (ice crust), which prevented the possible sticking of vegetable cubes when the internal moisture passed to the crystalline structure.…”
Section: The Basic Part Of the Studymentioning
confidence: 99%
“…Quantifying the influence of vertical cooling tubes' presence on hydrodynamics, heat, and mass transfer rates is needed for efficient design, scale-up, and operation of the fluidized bed reactor for the Fischer Tropsch process. This type of data is highly needed in the literature because the design and scale-up of these reactors equipped with a bundle of cooling tubes are still based on employing the correlations obtained from experimental data collected in fluidized bed reactors without vertical cooling tubes [14,18,[22][23][24]. In addition, significant literature contributions have reported on heat transfer in fluidized bed reactors [23][24][25][26].…”
Section: Introductionmentioning
confidence: 99%
“…The ratio between primary energy of produced syngas to biomass primary energy, defined as the efficiency of the gasification process, is generally in the range between 60% and 90% [52][53][54]. Bisht et al, in [52], analysed on a simulative basis a small-scale biomass gasification plant.…”
mentioning
confidence: 99%
“…Ribó-Pérez et al [53] simulated a gasifier power plant including an electric generator by means of HOMER software. Vargas-Salgado et al [54] designed, sized and experimentally analysed small-scale fluidised bed gasification plants. The system produces syngas with a gasifier efficiency in the range 59-82%.…”
mentioning
confidence: 99%