In a boundary wall of a pipe for developed laminar flow, to find the best example in which the least enthalpy and entropy are created, non-uniform distribution of convective flow in wall is studied. Some factors are simulated for transfer coefficient heat variations of moving the pipe. Distribution of temperature, entropy and enthalpy along the radius and distribution of generated entropy and enthalpy along the tube axis are shown. Entropy and enthalpy are reduced along the axis. Entropy, except some areas close to the wall, is increasing along the radius. Temperature and enthalpy, approaching the wall along the radius, have increased.
Published in | World Journal of Applied Chemistry (Volume 4, Issue 4) |
DOI | 10.11648/j.wjac.20190404.15 |
Page(s) | 69-78 |
Creative Commons |
This is an Open Access article, distributed under the terms of the Creative Commons Attribution 4.0 International License (http://creativecommons.org/licenses/by/4.0/), which permits unrestricted use, distribution and reproduction in any medium or format, provided the original work is properly cited. |
Copyright |
Copyright © The Author(s), 2019. Published by Science Publishing Group |
Generated Entropy, Enthalpy, Computational Fluid Dynamics
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APA Style
Reza Kakulvand. (2019). Effect of Non-uniform Convection on Entropy Generation and Enthalpy for the Laminar Developing Pipe Flow of a High Prandtl Number Fluid. World Journal of Applied Chemistry, 4(4), 69-78. https://doi.org/10.11648/j.wjac.20190404.15
ACS Style
Reza Kakulvand. Effect of Non-uniform Convection on Entropy Generation and Enthalpy for the Laminar Developing Pipe Flow of a High Prandtl Number Fluid. World J. Appl. Chem. 2019, 4(4), 69-78. doi: 10.11648/j.wjac.20190404.15
AMA Style
Reza Kakulvand. Effect of Non-uniform Convection on Entropy Generation and Enthalpy for the Laminar Developing Pipe Flow of a High Prandtl Number Fluid. World J Appl Chem. 2019;4(4):69-78. doi: 10.11648/j.wjac.20190404.15
@article{10.11648/j.wjac.20190404.15, author = {Reza Kakulvand}, title = {Effect of Non-uniform Convection on Entropy Generation and Enthalpy for the Laminar Developing Pipe Flow of a High Prandtl Number Fluid}, journal = {World Journal of Applied Chemistry}, volume = {4}, number = {4}, pages = {69-78}, doi = {10.11648/j.wjac.20190404.15}, url = {https://doi.org/10.11648/j.wjac.20190404.15}, eprint = {https://article.sciencepublishinggroup.com/pdf/10.11648.j.wjac.20190404.15}, abstract = {In a boundary wall of a pipe for developed laminar flow, to find the best example in which the least enthalpy and entropy are created, non-uniform distribution of convective flow in wall is studied. Some factors are simulated for transfer coefficient heat variations of moving the pipe. Distribution of temperature, entropy and enthalpy along the radius and distribution of generated entropy and enthalpy along the tube axis are shown. Entropy and enthalpy are reduced along the axis. Entropy, except some areas close to the wall, is increasing along the radius. Temperature and enthalpy, approaching the wall along the radius, have increased.}, year = {2019} }
TY - JOUR T1 - Effect of Non-uniform Convection on Entropy Generation and Enthalpy for the Laminar Developing Pipe Flow of a High Prandtl Number Fluid AU - Reza Kakulvand Y1 - 2019/11/19 PY - 2019 N1 - https://doi.org/10.11648/j.wjac.20190404.15 DO - 10.11648/j.wjac.20190404.15 T2 - World Journal of Applied Chemistry JF - World Journal of Applied Chemistry JO - World Journal of Applied Chemistry SP - 69 EP - 78 PB - Science Publishing Group SN - 2637-5982 UR - https://doi.org/10.11648/j.wjac.20190404.15 AB - In a boundary wall of a pipe for developed laminar flow, to find the best example in which the least enthalpy and entropy are created, non-uniform distribution of convective flow in wall is studied. Some factors are simulated for transfer coefficient heat variations of moving the pipe. Distribution of temperature, entropy and enthalpy along the radius and distribution of generated entropy and enthalpy along the tube axis are shown. Entropy and enthalpy are reduced along the axis. Entropy, except some areas close to the wall, is increasing along the radius. Temperature and enthalpy, approaching the wall along the radius, have increased. VL - 4 IS - 4 ER -