Conical spouted beds for waste valorization: Assessment of particle segregation in beds composed of sand and Tetra Pak residues

2021 ◽  
Vol 47 ◽  
pp. 101334
Author(s):  
Diunay Zuliani Mantegazini ◽  
Thiago Padovani Xavier ◽  
Marcelo Silveira Bacelos
1983 ◽  
Vol 61 (3) ◽  
pp. 308-316 ◽  
Author(s):  
E. Kutluoglu ◽  
J. R. Grace ◽  
K. W. Murchie ◽  
P. H. Cavanagh

1992 ◽  
Vol 57 (10) ◽  
pp. 2100-2112 ◽  
Author(s):  
Vladimír Kudrna ◽  
Pavel Hasal ◽  
Andrzej Rochowiecki

A process of segregation of two distinct fractions of solid particles in a rotating horizontal drum mixer was described by stochastic model assuming the segregation to be a diffusion process with varying diffusion coefficient. The model is based on description of motion of particles inside the mixer by means of a stochastic differential equation. Results of stochastic modelling were compared to the solution of the corresponding Kolmogorov equation and to results of earlier carried out experiments.


2020 ◽  
Vol 309 ◽  
pp. 123400 ◽  
Author(s):  
M. Venkateswar Reddy ◽  
Gopalakrishnan Kumar ◽  
Gunda Mohanakrishna ◽  
Sutha Shobana ◽  
Riyadh I. Al-Raoush

Author(s):  
Heng Zhou ◽  
Shuyu Wang ◽  
Binbin Du ◽  
Mingyin Kou ◽  
Zhiyong Tang ◽  
...  

AbstractIn order to develop the central gas flow in COREX shaft furnace, a new installment of center gas supply device (CGD) is designed. In this work, a coupled DEM–CFD model was employed to study the influence of CGD on gas–solid flow in COREX shaft furnace. The particle descending velocity, particle segregation behaviour, void distribution and gas distribution were investigated. The results show that the CGD affects the particles descending velocity remarkably as the burden falling down to the slot. Particle segregation can be observed under the inverse ‘V’ burden profile, and the influence of CGD on the particle segregation is unobvious on the whole, which causes the result that the voidage is slightly changed. Although the effect of CGD on solid flow is not significant, the gas flow in shaft furnace has an obvious change. Compared with the condition without CGD, in the case with CGD, the gas velocity is improved significantly, especially in the middle zone of the furnace, which further promotes the center gas distribution. Meanwhile, the pressure drop in the furnace with the installation of CGD is increased partly.


2021 ◽  
Author(s):  
Idoia Hita del Olmo ◽  
Subram Mani Sarathy ◽  
Pedro Castaño

The valorization of polymeric waste, such as biomass, tires, and plastics, via thermal depolymerization (i.e., pyrolysis and liquefaction) and simultaneous or subsequent catalytic treatment has gained enormous momentum. The inherent...


2020 ◽  
Vol 2 (4) ◽  
Author(s):  
Ryan P. Jones ◽  
Julio M. Ottino ◽  
Paul B. Umbanhowar ◽  
Richard M. Lueptow

2021 ◽  
Vol 12 (1) ◽  
Author(s):  
Zhi-Hua Liu ◽  
Naijia Hao ◽  
Yun-Yan Wang ◽  
Chang Dou ◽  
Furong Lin ◽  
...  

AbstractBiological lignin valorization has emerged as a major solution for sustainable and cost-effective biorefineries. However, current biorefineries yield lignin with inadequate fractionation for bioconversion, yet substantial changes of these biorefinery designs to focus on lignin could jeopardize carbohydrate efficiency and increase capital costs. We resolve the dilemma by designing ‘plug-in processes of lignin’ with the integration of leading pretreatment technologies. Substantial improvement of lignin bioconversion and synergistic enhancement of carbohydrate processing are achieved by solubilizing lignin via lowering molecular weight and increasing hydrophilic groups, addressing the dilemma of lignin- or carbohydrate-first scenarios. The plug-in processes of lignin could enable minimum polyhydroxyalkanoate selling price at as low as $6.18/kg. The results highlight the potential to achieve commercial production of polyhydroxyalkanoates as a co-product of cellulosic ethanol. Here, we show that the plug-in processes of lignin could transform biorefinery design toward sustainability by promoting carbon efficiency and optimizing the total capital cost.


2021 ◽  
Vol 6 (8) ◽  
pp. 1814-1822
Author(s):  
Hanxin Huo ◽  
Yuhui Ma ◽  
Xunliang Wang
Keyword(s):  

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