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Pipe flow of homogeneous slurryHallbom, Donald John 11 1900 (has links)
The objective of this Thesis is to devise a system for the "rheology-based design" of non-settling (homogeneous) slurry pipelines that is more conducive to application by practicing engineers without impairing its accuracy or utility for research purposes. The cornerstone is the development of a new rheological model and constitutive equation for homogeneous slurry based on the aggregation/deaggregation of the suspended mineral particles. This “yield plastic” model is shown to describe a family of models that includes the Newtonian, Bingham plastic and Casson models as special cases. It also closely approximates the results of many consistency models, including power law, yield power law, Cross and Carreau-Yasuda.
The yield plastic model is then used to develop design equations to determine the pressure-gradient of laminar and turbulent pipe flow. A relative energy dissipation criterion is proposed for the laminar-turbulent transition and shown to be consistent with currently used transition models for Newtonian and Bingham fluids. Finally, a new dimensionless group (the “stress number”) is proposed that is directly proportional to the pressure-gradient and independent of the velocity. When the design equations are presented graphically in terms of the stress number and the plastic Reynolds number, the resulting “design curve diagram” is shown to be a dimensionless (pressure-gradient vs. velocity) pipe flow curve.
The net result is that the hydraulic design of homogeneous slurry systems only requires the use of a single constitutive equation and three engineering design equations. The results are presented in a conceptually easy form that will foster an intuitive understanding of non-Newtonian pipe flow. This will assist engineers to understand the impact of slurry rheology when designing, operating and troubleshooting slurry pipelines and, in the future, other slurry related processes.
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Pipe flow of homogeneous slurryHallbom, Donald John 11 1900 (has links)
The objective of this Thesis is to devise a system for the "rheology-based design" of non-settling (homogeneous) slurry pipelines that is more conducive to application by practicing engineers without impairing its accuracy or utility for research purposes. The cornerstone is the development of a new rheological model and constitutive equation for homogeneous slurry based on the aggregation/deaggregation of the suspended mineral particles. This “yield plastic” model is shown to describe a family of models that includes the Newtonian, Bingham plastic and Casson models as special cases. It also closely approximates the results of many consistency models, including power law, yield power law, Cross and Carreau-Yasuda.
The yield plastic model is then used to develop design equations to determine the pressure-gradient of laminar and turbulent pipe flow. A relative energy dissipation criterion is proposed for the laminar-turbulent transition and shown to be consistent with currently used transition models for Newtonian and Bingham fluids. Finally, a new dimensionless group (the “stress number”) is proposed that is directly proportional to the pressure-gradient and independent of the velocity. When the design equations are presented graphically in terms of the stress number and the plastic Reynolds number, the resulting “design curve diagram” is shown to be a dimensionless (pressure-gradient vs. velocity) pipe flow curve.
The net result is that the hydraulic design of homogeneous slurry systems only requires the use of a single constitutive equation and three engineering design equations. The results are presented in a conceptually easy form that will foster an intuitive understanding of non-Newtonian pipe flow. This will assist engineers to understand the impact of slurry rheology when designing, operating and troubleshooting slurry pipelines and, in the future, other slurry related processes.
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Pipe flow of homogeneous slurryHallbom, Donald John 11 1900 (has links)
The objective of this Thesis is to devise a system for the "rheology-based design" of non-settling (homogeneous) slurry pipelines that is more conducive to application by practicing engineers without impairing its accuracy or utility for research purposes. The cornerstone is the development of a new rheological model and constitutive equation for homogeneous slurry based on the aggregation/deaggregation of the suspended mineral particles. This “yield plastic” model is shown to describe a family of models that includes the Newtonian, Bingham plastic and Casson models as special cases. It also closely approximates the results of many consistency models, including power law, yield power law, Cross and Carreau-Yasuda.
The yield plastic model is then used to develop design equations to determine the pressure-gradient of laminar and turbulent pipe flow. A relative energy dissipation criterion is proposed for the laminar-turbulent transition and shown to be consistent with currently used transition models for Newtonian and Bingham fluids. Finally, a new dimensionless group (the “stress number”) is proposed that is directly proportional to the pressure-gradient and independent of the velocity. When the design equations are presented graphically in terms of the stress number and the plastic Reynolds number, the resulting “design curve diagram” is shown to be a dimensionless (pressure-gradient vs. velocity) pipe flow curve.
The net result is that the hydraulic design of homogeneous slurry systems only requires the use of a single constitutive equation and three engineering design equations. The results are presented in a conceptually easy form that will foster an intuitive understanding of non-Newtonian pipe flow. This will assist engineers to understand the impact of slurry rheology when designing, operating and troubleshooting slurry pipelines and, in the future, other slurry related processes. / Applied Science, Faculty of / Mining Engineering, Keevil Institute of / Graduate
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A Dredging Knowledge-Base Expert System for Pipeline Dredges with Comparison to Field DataWilson, Derek Alan 2010 December 1900 (has links)
A Pipeline Analytical Program and Dredging Knowledge{Base Expert{System
(DKBES) determines a pipeline dredge's production and resulting cost and schedule.
Pipeline dredge engineering presents a complex and dynamic process necessary to
maintain navigable waterways. Dredge engineers use pipeline engineering and slurry
transport principles to determine the production rate of a pipeline dredge system.
Engineers then use cost engineering factors to determine the expense of the dredge
project.
Previous work in engineering incorporated an object{oriented expert{system to
determine cost and scheduling of mid{rise building construction where data objects
represent the fundamental elements of the construction process within the program
execution. A previously developed dredge cost estimating spreadsheet program which
uses hydraulic engineering and slurry transport principles determines the performance
metrics of a dredge pump and pipeline system. This study focuses on combining
hydraulic analysis with the functionality of an expert{system to determine the performance
metrics of a dredge pump and pipeline system and its resulting schedule.
Field data from the U.S. Army Corps of Engineers pipeline dredge, Goetz, and
several contract daily dredge reports show how accurately the DKBES can predict
pipeline dredge production. Real{time dredge instrumentation data from the Goetz compares the accuracy of the Pipeline Analytical Program to actual dredge operation.
Comparison of the Pipeline Analytical Program to pipeline daily dredge reports
shows how accurately the Pipeline Analytical Program can predict a dredge project's
schedule over several months. Both of these comparisons determine the accuracy
and validity of the Pipeline Analytical Program and DKBES as they calculate the
performance metrics of the pipeline dredge project.
The results of the study determined that the Pipeline Analytical Program compared
closely to the Goetz eld data where only pump and pipeline hydraulics a ected
the dredge production. Results from the dredge projects determined the Pipeline Analytical
Program underestimated actual long{term dredge production. Study results
identi ed key similarities and di erences between the DKBES and spreadsheet program
in terms of cost and scheduling. The study then draws conclusions based on
these ndings and o ers recommendations for further use.
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