scholarly journals Performance evaluation of solar flat plate collector using different working fluids through computational fluid dynamics

2020 ◽  
Vol 2 (2) ◽  
Author(s):  
Imran Nazir Unar ◽  
Ghulamullah Maitlo ◽  
Shoaib Ahmed ◽  
Syed Saad Ali ◽  
Abdul Qayoom Memon ◽  
...  
Author(s):  
Mohammed Amine Amraoui ◽  
Khaled Aliane

This paper presents the study of fluid flow and heat transfer in solar flat plate collector by using Computational Fluid Dynamics (CFD) which reduces time and cost. In the present paper the computational fluid dynamics (CFD) tool has been used to simulate the solar collector for better understanding the heat transfer capability. 3D model of the collector involving air inlet, the collector is modeled by ANSYS Workbench and the grid was created in ANSYS ICEM. The results were obtained by using ANSYS FLUENT and ANSYS CFX. The objective of this work is to compare theoretically and experimentally work done with the work done by using computational fluid dynamics (CFD) tool with respect to flow and temperature distribution inside the solar collector. The outlet temperature of air is compared with experimental results and there is a good agreement in between them.


2020 ◽  
Vol 43 (10) ◽  
Author(s):  
Onkar A Babar ◽  
Ayon Tarafdar ◽  
Santanu Malakar ◽  
Vinkel Kumar Arora ◽  
Prabhat K. Nema

2019 ◽  
Vol 151 ◽  
pp. 107257 ◽  
Author(s):  
Camila Larissa Hinterholz ◽  
Daniela Estelita Goes Trigueros ◽  
Aparecido Nivaldo Módenes ◽  
Carlos Eduardo Borba ◽  
Fabiano Bisinella Scheufele ◽  
...  

Author(s):  
K Vijayaraj ◽  
Punit Singh

Many new turbine designs may take large timelines to prove their worth. For getting duty condition at optimum efficiency, one can always scale speed, diameter, if a very efficient benchmark is available. This paper examines the similarity-based scaling strategy to develop radial inflow turbines for different compressible fluids from a well-established NASA radial flow turbine designed and experimentally tested with air as the working fluid. The NASA 1730 air turbine experimental data have been used as the benchmark here and adopted multiple fluids to understand scaling. The considered fluids are supercritical carbon dioxide for the Brayton cycle, helium for the cryogenic liquefaction cycle, and R143a for the organic Rankine cycle. The uniqueness here is to have three types of cycles, viz. closed-loop Brayton cycle, organic Rankine cycle, and cryogenic helium liquefaction cycle, which employ different working fluids, adapting the same NASA turbine geometry. This paper has described the scaling methodology and presented the simulated turbine performance of SCO2, helium, and R143a using computational fluid dynamics. The dimensionless curves for these fluids are plotted on the corresponding experimental characteristics of the NASA turbine. Out of the three fluids, SCO2 showed the perfect Mach number matching for the flow and torque coefficient curves. The Mach number deviations in the case of helium were small, and the variations were slightly higher for R143a. The efficiencies were the highest for R143a, followed by SCO2 and helium. Thus, the scaling was found to be effective in all cases. Thus, the standard turbomachinery space developed for air as fluid can be used effectively for the development of turboexpanders for various cycles with different working fluids without redesigning the entire shape using similarity-based scaling. The benchmark NASA 1730 turbine has proven this in three special cases. This paper is not against designing new machines but is only trying to say that when such good benchmark machines like NASA 1730 turbine is available; designers must use the power of similitude to adapt it to match new fluids and new conditions.


Author(s):  
M. T. F. Owen ◽  
D. G. Kröger

The development of an efficient and reliable method of evaluating the performance of an air-cooled steam condenser (ACC) under windy conditions using computational fluid dynamics (CFD) is presented. A two-step modeling approach is employed as a result of computational limitations. The numerical ACC model developed in this study makes use of the pressure jump fan model, among other approximations, in an attempt to minimize the computational expense of the performance evaluation. The accuracy of the numerical model is verified through a comparison of the numerical results to test data collected during full-scale tests carried out on an operational ACC. Good correlation is achieved between the numerical results and test data. The effect of wind on ACC performance at El Dorado Power Plant (Nevada, USA) is investigated. It is found that reduced fan performance due to distorted flow at the inlet of the upstream fans is the primary contributor to the reduction in ACC performance associated with increased wind speed in this case. The model developed in this study has the potential to allow for the evaluation of large ACC installations and provides a reliable platform from which further investigations into improving ACC performance under windy conditions can be carried out.


2013 ◽  
Vol 10 (6) ◽  
Author(s):  
Susanta K. Das ◽  
Kranthi K. Gadde

A catalytic flat plate fuel reformer offers better heat integration by combining the exothermic catalytic combustion reaction on one side and the endothermic catalytic reforming reaction on the other side. In this study, steam reforming of natural gas (methane) coupled with a methane catalytic combustion in a catalytic flat plate reformer is studied using a two-dimensional model for a cocurrent flow arrangement. The two-dimensional computational fluid dynamics (CFD) model makes the predictions more realistic by increasing its capability to capture the effect of various design parameters and eliminates the uncertainties introduced by heat and mass transfer coefficients used in one-dimensional models. In our work we simulated the entire catalytic flat plate reformer (both reforming side and combustion side) and carried-out studies related to important design parameters such as channel height, inlet fuel velocities, and catalyst layer thickness that can provide guidance for the practical implementation of such fuel reformer design. The simulated transverse temperature profiles (not shown here due to page limitation) show that there is virtually no heat loss across the plate at the reformer exit. Introduction of a water gas shift (WGS) reaction at the reformer side along with our optimized reformer design parameters decreases the amount of carbon monoxide (CO) almost 90%–98% in the final reformate exiting the reformer as compared to without the WGS reaction. The CFD results obtained in this study will be very helpful to understand the optimization of design parameters to build a first generation prototype.


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