東華大學圖書館 |

Modeling of Non-Newtonian Fluid Flow in a Porous Medium.

紀錄類型:	書目-電子資源 : Monograph/item
正題名/作者:	Modeling of Non-Newtonian Fluid Flow in a Porous Medium./
作者:	Azzam, Hamza.
面頁冊數:	1 online resource (85 pages)
附註:	Source: Masters Abstracts International, Volume: 83-03.
Contained By:	Masters Abstracts International83-03.
標題:	Petroleum engineering. -
電子資源:	http://pqdd.sinica.edu.tw/twdaoapp/servlet/advanced?query=28681273click for full text (PQDT)
ISBN:	9798544202936

Modeling of Non-Newtonian Fluid Flow in a Porous Medium.
Azzam, Hamza.

Modeling of Non-Newtonian Fluid Flow in a Porous Medium. - 1 online resource (85 pages)

Source: Masters Abstracts International, Volume: 83-03.

Thesis (M.Sc.)--The University of Maine, 2020.

Includes bibliographical references

Flows of Newtonian and non-Newtonian fluids in porous media are of considerable interest in several diverse areas, including petroleum engineering, chemical engineering, and composite materials manufacturing.In the first part of this thesis, one-dimensional linear and radial isothermal infiltration models for a non-Newtonian fluid flow in a porous solid preform are presented. The objective is to investigate the effects of the flow behavior index, preform porosity and the inlet boundary condition (which is either a known applied pressure or a fluid flux factor) on the infiltration front, pore pressure distribution, and fluid content variation. In the second part of the thesis, a onedimensional linear non-isothermal infiltration model for a Newtonian fluid is presented. The goal is to investigate the effects of convection heat transfer and the applied boundary conditions, which are the applied pressure and the inlet temperature, on the infiltration front, pore pressure distribution, temperature variation, and fluid content variation.For all types of infiltrations studied in this thesis, the governing equations for the threedimensional (3D) infiltration are first presented. The 3D equations are then reduced to those for one-dimensional (1D) flow. After that, self-similarity solutions are derived for the various types of 1D flows. Finally, numerical results are presented and discussed for a ceramic solid preform infiltrated by a melted polymer liquid. The theoretical models and numerical results show that1. For 1-D linear isothermal infiltration of a non-Newtonian fluid, the dimensional infiltration front varies with time according to n/tn+1, where n is the flow behavior index. The dimensionless infiltration front increases with an increase in the flow behavior index \uD835\uDC5B, and decreases with an increase in the porosity of the porous solid. The pore pressure varies almost linearly from the inlet to the infiltration front. The fluid content variation becomes negative when the non-dimensional distance reaches about 55% of the infiltration front.2. For 1-D radial isothermal infiltration of a non-Newtonian fluid, the dimensional infiltration front varies with time according to n/tn+1. The dimensionless infiltration front increases with an increase in the flow behavior index n, and decreases with an increase in the porosity of the porous solid. The pore pressure varies non-linearly from the inlet and reaches zero at the infiltration front.3. The fluid travels farther in the linear infiltration than in the radial infiltration.4. For 1-D linear non-isothermal infiltration of a Newtonian fluid, the dimensional infiltration front varies with time according to t1/2. It appears that the convection has a negligible effect on the infiltration front and the pore pressure distribution. The infiltration front increases with a decrease in the porosity of the porous solid. The pore pressure varies almost linearly from the inlet to the infiltration front, where it reaches zero. With an applied temperature drop at the inlet, the temperature variation increases with increasing distance from the inlet and reaches zero at a distance farther than the infiltration front, not at the infiltration front.

Electronic reproduction.
Ann Arbor, Mich. :
ProQuest,
2023

Mode of access: World Wide Web

ISBN: 9798544202936Subjects--Topical Terms:

566616
Petroleum engineering.
Index Terms--Genre/Form:

542853
Electronic books.

Modeling of Non-Newtonian Fluid Flow in a Porous Medium.
LDR:04552nmm a2200397K 4500 001 2353870
005 20230322053925.5
006 m o d
007 cr mn ---uuuuu
008 241011s2020 xx obm 000 0 eng d
020 $a 9798544202936
035 $a (MiAaPQ)AAI28681273
035 $a (MiAaPQ)U_Maine4438
035 $a AAI28681273
040 $a MiAaPQ $b eng $c MiAaPQ $d NTU
100 1 $a Azzam, Hamza. $3 3694201
245 1 0 $a Modeling of Non-Newtonian Fluid Flow in a Porous Medium.
264 0 $c 2020
300 $a 1 online resource (85 pages)
336 $a text $b txt $2 rdacontent
337 $a computer $b c $2 rdamedia
338 $a online resource $b cr $2 rdacarrier
500 $a Source: Masters Abstracts International, Volume: 83-03.
500 $a Advisor: Jin, Zhihe; Kimball, Richard; Yang, Yingchao.
502 $a Thesis (M.Sc.)--The University of Maine, 2020.
504 $a Includes bibliographical references
520 $a Flows of Newtonian and non-Newtonian fluids in porous media are of considerable interest in several diverse areas, including petroleum engineering, chemical engineering, and composite materials manufacturing.In the first part of this thesis, one-dimensional linear and radial isothermal infiltration models for a non-Newtonian fluid flow in a porous solid preform are presented. The objective is to investigate the effects of the flow behavior index, preform porosity and the inlet boundary condition (which is either a known applied pressure or a fluid flux factor) on the infiltration front, pore pressure distribution, and fluid content variation. In the second part of the thesis, a onedimensional linear non-isothermal infiltration model for a Newtonian fluid is presented. The goal is to investigate the effects of convection heat transfer and the applied boundary conditions, which are the applied pressure and the inlet temperature, on the infiltration front, pore pressure distribution, temperature variation, and fluid content variation.For all types of infiltrations studied in this thesis, the governing equations for the threedimensional (3D) infiltration are first presented. The 3D equations are then reduced to those for one-dimensional (1D) flow. After that, self-similarity solutions are derived for the various types of 1D flows. Finally, numerical results are presented and discussed for a ceramic solid preform infiltrated by a melted polymer liquid. The theoretical models and numerical results show that1. For 1-D linear isothermal infiltration of a non-Newtonian fluid, the dimensional infiltration front varies with time according to n/tn+1, where n is the flow behavior index. The dimensionless infiltration front increases with an increase in the flow behavior index \uD835\uDC5B, and decreases with an increase in the porosity of the porous solid. The pore pressure varies almost linearly from the inlet to the infiltration front. The fluid content variation becomes negative when the non-dimensional distance reaches about 55% of the infiltration front.2. For 1-D radial isothermal infiltration of a non-Newtonian fluid, the dimensional infiltration front varies with time according to n/tn+1. The dimensionless infiltration front increases with an increase in the flow behavior index n, and decreases with an increase in the porosity of the porous solid. The pore pressure varies non-linearly from the inlet and reaches zero at the infiltration front.3. The fluid travels farther in the linear infiltration than in the radial infiltration.4. For 1-D linear non-isothermal infiltration of a Newtonian fluid, the dimensional infiltration front varies with time according to t1/2. It appears that the convection has a negligible effect on the infiltration front and the pore pressure distribution. The infiltration front increases with a decrease in the porosity of the porous solid. The pore pressure varies almost linearly from the inlet to the infiltration front, where it reaches zero. With an applied temperature drop at the inlet, the temperature variation increases with increasing distance from the inlet and reaches zero at a distance farther than the infiltration front, not at the infiltration front.
533 $a Electronic reproduction. $b Ann Arbor, Mich. : $c ProQuest, $d 2023
538 $a Mode of access: World Wide Web
650 4 $a Petroleum engineering. $3 566616
650 4 $a Pollutants. $3 551065
650 4 $a Manufacturing. $3 3389707
650 4 $a Solidification. $3 699781
650 4 $a Environmental engineering. $3 548583
650 4 $a Numerical analysis. $3 517751
650 4 $a Heat conductivity. $3 3681489
650 4 $a Composite materials. $3 654082
650 4 $a Contamination. $3 3681972
650 4 $a Non-Newtonian fluids. $3 626381
650 4 $a Heat transfer. $3 3391367
650 4 $a Polymers. $3 535398
650 4 $a Velocity. $3 3560495
650 4 $a Partial differential equations. $3 2180177
650 4 $a Viscosity. $3 1050706
650 4 $a Rheology. $3 570780
650 4 $a Permeability. $3 915594
650 4 $a Fractures. $3 823229
650 4 $a Engineering. $3 586835
650 4 $a Deformation. $2 lcstt $3 3267001
650 4 $a Geometry. $3 517251
650 4 $a Solids. $3 578759
650 4 $a Interfaces. $2 gtt $3 834756
650 4 $a Industrial engineering. $3 526216
650 4 $a Mechanical engineering. $3 649730
650 4 $a Mechanics. $3 525881
650 4 $a Mathematics. $3 515831
650 4 $a Random variables. $3 646291
650 4 $a Efficiency. $3 753744
655 7 $a Electronic books. $2 lcsh $3 542853
690 $a 0765
690 $a 0775
690 $a 0537
690 $a 0546
690 $a 0548
690 $a 0346
690 $a 0405
710 2 $a ProQuest Information and Learning Co. $3 783688
710 2 $a The University of Maine. $3 1029373
773 0 $t Masters Abstracts International $g 83-03.
856 4 0 $u http://pqdd.sinica.edu.tw/twdaoapp/servlet/advanced?query=28681273 $z click for full text (PQDT)