2017
DOI: 10.1016/j.powtec.2017.01.039
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Experimental quantification of the head loss coefficient K for fittings and semi-industrial pipe cross section solid concentration profile in pneumatic conveying of polypropylene pellets in dilute phase

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Cited by 18 publications
(14 citation statements)
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“…K = 4,97398 v (-0,538827) (2) Sendo K o fator multiplicador da carga cinética (adimensional) e v a velocidade do ar em m/s para vazões de poliestireno de 114,84 até 325,87 kg/h. Os valores de K obtidos com o polipropileno por Moraes et al (2017) foram, para as mesmas condições experimentais, inferiores ao do presente estudo com o poliestireno em função da geometria das partículas.…”
Section: Resultsunclassified
See 1 more Smart Citation
“…K = 4,97398 v (-0,538827) (2) Sendo K o fator multiplicador da carga cinética (adimensional) e v a velocidade do ar em m/s para vazões de poliestireno de 114,84 até 325,87 kg/h. Os valores de K obtidos com o polipropileno por Moraes et al (2017) foram, para as mesmas condições experimentais, inferiores ao do presente estudo com o poliestireno em função da geometria das partículas.…”
Section: Resultsunclassified
“…As vazões de poliestireno da presente pesquisa foram as mesmas fixadas por Moraes, et al (2017) para o polipropileno (esferas com diâmetro aproximado de 3 mm) ou seja: 114,84; 219,69 e 325,87 kg/h. Quantificou-se através de um anemômetro as velocidades no duto de sucção do ventilador.…”
Section: Processo Operacionalunclassified
“…The use of empirical procedures [7,9,16] cannot provide a complete calculation of the installations, including changes in the characteristics of a two-component flow under different installation's modes of operation [17][18][19]. Using the most general theoretical description of the pneumatic conveying process mentioned in papers [1,8], objective difficulties associated with a complicated system of equations [4,5] in features of the control system with controlled feedback.…”
Section: Literature Review and Problem Statementmentioning
confidence: 99%
“…The different formulation for different gas volume fraction as in equations (5)(6)(7)(8) follows the suggestion of Gidaspow [24]. The turbulent dispersion force , in equation 2is modelled with the FAD model [30] that is included in the software, according to equations (9-10)…”
Section: Governing Equationsmentioning
confidence: 99%
“…Due to their complexities, experimental studies are still being conducted to study pneumatic conveying processes. Some examples will include work by Khan et al [5] on the pick-up velocity of particles and de Moraes et al [6] on head loss coefficient for pipe fittings, both of which deal with properties fundamental to pneumatic conveying processes. While experimental studies form a significant portion of pneumatic conveying investigations, the number of numerical simulation studies are increasing as well.…”
Section: Introductionmentioning
confidence: 99%