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Double-diffusive natural convection and entropy generation of Bingham fluid in an inclined cavity

机译:斜腔内宾汉流体的双扩散自然对流和熵产生

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In this paper, double-diffusive natural convection, studying Soret and Dufour effects and viscous dissipation in a square cavity filled with Bingham fluid has been simulated by Finite Difference Lattice Boltzmann Method (FDLBM). In addition, entropy generations through fluid friction, heat transfer, and mass transfer has been studied. The problem has been solved by applying the regularised Papanastasiou model. This study has been conducted for certain pertinent parameters of Rayleigh number (Ra = 10~3, 10~4 and 10~5), Bingham number (Bn), Lewis number (Le = 2.5, 5 and 10), Dufour parameter (D_f = 0, 1, and 5), Soret parameter (S_r = 0, 1, and 5), Eckert number (E_C = 0, 0.001, and 0.01), inclined angle (θ = 0, 40, 80, and 120) and the Buoyancy ratio (N= -1, 0.1, 1). Results indicate that the increase in Rayleigh number enhances heat and mass transfer for various Bingham numbers and inclined angles. The alteration of the inclined angle changes heat and mass transfer. In addition, the rise of the inclined angle alter the unyielded zones. The increase in the Lewis number augments mass transfer in different inclined angles while it causes heat transfer to drop marginally at θ = 0, 40, and 120. The heat transfer increases with the rise of the Dufour parameter and the mass transfer enhances as the Soret parameter increases for different Bingham numbers and Rayleigh numbers. In some cases, the augmentation of Soret and Dufour parameters alter the behavior of heat and mass transfer against the alteration of the inclined angle. The addition of Soret and Dufour parameters and Lewis numbers do not affect the unyielded zone considerably. The augmentation of the buoyancy ratio number enhances heat and mass transfer. The rise of buoyancy ratio number alters the unyielded section significantly. The increase in Eckert number declines heat transfer, but it has a marginal effect on mass transfer. The augmentation of Rayleigh number enhances different entropy generations and declines the average Bejan number. The increase in the Bingham number provokes various irreversibilities to drop significantly. The rise of Soret and Dufour parameters enhances the entropy generations due to heat transfer and fluid friction. The rise of Eckert number alters various entropy generations, but the alteration does not follow a specific manner in different studied parameters.
机译:在本文中,通过有限差分格子玻尔兹曼方法(FDLBM)模拟了双扩散自然对流,研究了在充满Bingham流体的方腔中的Soret和Dufour效应以及粘性耗散。另外,已经研究了通过流体摩擦,热传递和质量传递产生的熵。通过应用正则化Papanastasiou模型已解决了该问题。本研究针对瑞利数(Ra = 10〜3、10〜4和10〜5),宾厄姆数(Bn),路易斯数(Le = 2.5、5和10),杜福尔参数(D_f)的某些相关参数进行= 0、1和5),Soret参数(S_r = 0、1和5),埃克特数(E_C = 0、0.001和0.01),倾斜角(θ= 0、40、80和120)和浮力比(N = -1,0.1,1)。结果表明,瑞利数的增加增强了各种宾汉数和倾斜角的传热和传质。倾斜角的改变改变了传热和传质。另外,倾斜角的上升改变了未屈服区域。 Lewis数的增加会增加不同倾斜角度的传质,同时导致传热在θ= 0、40和120时略有下降。传热随着Dufour参数的增加而增加,传质随着Soret的增加而增强对于不同的Bingham数和Rayleigh数,参数增加。在某些情况下,Soret和Dufour参数的增加会改变热和传质的行为,而不会改变倾斜角度。 Soret和Dufour参数以及Lewis数的相加不会显着影响未屈服区。浮力比数的增加增强了传热和传质。浮力比数的增加极大地改变了未屈服的部分。 Eckert数的增加会降低传热,但对传质影响很小。瑞利数的增加增强了不同熵的产生,并降低了平均贝扬数。 Bingham数的增加导致各种不可逆性显着下降。 Soret和Dufour参数的上升会由于传热和流体摩擦而增加熵的产生。 Eckert数的增加改变了各种熵的产生,但是在不同的研究参数中,这种改变并未遵循特定的方式。

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