| Literature DB >> 33286228 |
Iskander Tlili1,2, Sania Naseer3, Muhammad Ramzan3,4, Seifedine Kadry5, Yunyoung Nam6.
Abstract
This article elucidates the magnetohydrodynamic 3D Maxwell nanofluid flow with heat absorption/generation effects. The impact of the nonlinear thermal radiation with a chemical reaction is also an added feature of the presented model. The phenomenon of flow is supported by thermal and concentration stratified boundary conditions. The boundary layer set of non-linear PDEs (partial differential equation) are converted into ODEs (ordinary differential equation) with high nonlinearity via suitable transformations. The homotopy analysis technique is engaged to regulate the mathematical analysis. The obtained results for concentration, temperature and velocity profiles are analyzed graphically for various admissible parameters. A comparative statement with an already published article in limiting case is also added to corroborate our presented model. An excellent harmony in this regard is obtained. The impact of the Nusselt number for distinct parameters is also explored and discussed. It is found that the impacts of Brownian motion on the concentration and temperature distributions are opposite. It is also comprehended that the thermally stratified parameter decreases the fluid temperature.Entities:
Keywords: Maxwell nanofluid; chemical reaction; double stratification; nonlinear thermal radiation
Year: 2020 PMID: 33286228 PMCID: PMC7516935 DOI: 10.3390/e22040453
Source DB: PubMed Journal: Entropy (Basel) ISSN: 1099-4300 Impact factor: 2.524
Figure 1Schematic 3D flow.
The analytical solution’s convergence for varying order of approximations while , , , , , , , , , and .
| Approximations Order |
|
|
|
|
|---|---|---|---|---|
| 1 | 0.99750 | 0.15980 | 0.13620 | 0.18150 |
| 5 | 1.00200 | 0.15390 | 0.09212 | 0.20190 |
| 10 | 0.99880 | 0.15360 | 0.07378 | 0.21070 |
| 20 | 0.99660 | 0.15400 | 0.06439 | 0.21430 |
| 25 | 0.99660 | 0.15400 | 0.06439 | 0.21430 |
Figure 2- curves for .
Figure 3Change of versus .
Figure 4Change of versus .
Figure 5Change of versus .
Figure 6Change of versus .
Figure 7Change of versus .
Figure 8Change of versus .
Figure 9Change of versus .
Figure 10Change of versus .
Figure 11Change of versus .
Figure 12Change of versus .
Figure 13Change of versus .
Figure 14Change of versus .
Figure 15Change of versus .
Figure 16Change of versus .
Figure 17Change of versus .
Figure 18Change of versus .
Figure 19Change of versus .
Figure 20Change of versus .
Figure 21Change of versus .
Figure 22Change of and on skin friction.
Figure 23Change of and on skin friction.
Figure 24Change of versus and .
Comparison with Bilal et al. [71] for the values of temperature gradient versus varied estimates of , , , , and in limiting case.
|
|
|
|
|
| ||||||
|---|---|---|---|---|---|---|---|---|---|---|
|
|
|
|
| |||||||
| Reference [ | Present | Reference [ | Present | Reference [ | Present | Reference [ | Present | |||
| 1 | 0.5 | 2 | 1.0169493 | 1.0169463 | 0.6127148 | 0.6127137 | 0.5395022 | 0.5395012 | 0.3170918 | 0.3170911 |
| 4 | 1.6016506 | 1.6016498 | 1.0169493 | 1.0169473 | 0.9034844 | 0.9034812 | 0.5510692 | 0.5510653 | ||
| 7 | 2.2439298 | 2.2439277 | 1.4727082 | 1.4727065 | 1.3143535 | 0.3143525 | 0.8208336 | 0.8208313 | ||
| 10 | 2.7550740 | 2.7550733 | 1.8369216 | 1.8369208 | 1.6428361 | 1.6428345 | 1.0373929 | 1.0373912 | ||
| 1 | 0 | 7 | 1.8260260 | 1.8260243 | 1.2025347 | 1.2025333 | 1.0737145 | 1.0737134 | 0.6725491 | 0.6725478 |
| 0.3 | 2.0940290 | 2.0940256 | 1.3782398 | 1.3782376 | 1.2305095 | 1.2305067 | 0.7701323 | 0.7701314 | ||
| 0.6 | 2.3129240 | 2.3129212 | 1.5154397 | 1.5154387 | 1.3609931 | 1.3609911 | 0.8434082 | 0.8434046 | ||
| 1 | 2.5591800 | 2.5591777 | 1.6644187 | 1.6644165 | 1.4836290 | 1.4836267 | 0.9204030 | 0.9204012 | ||
| 0 | 0.5 | 7 | 2.3543502 | 2.3543499 | 1.5922506 | 1.5302056 | 1.4275931 | 1.4275911 | 0.9108748 | 0.9108735 |
| 0.5 | 2.2966491 | 2.2966478 | 1.5302076 | 1.5302054 | 1.3684014 | 1.3684004 | 0.8638003 | 0.8638000 | ||
| 1.0 | 2.2439499 | 2.2439477 | 1.4727082 | 1.4727057 | 1.3143533 | 1.3143501 | 0.8208334 | 0.8208325 | ||
| 1.5 | 2.1950047 | 2.1950034 | 1.4200796 | 1.4200773 | 1.2649215 | 1.2649201 | 0.7818260 | 0.7818245 | ||