Author: Derrick J. Ryan
Publisher:
ISBN:
Category :
Languages : en
Pages :
Book Description
Numerical Study of Laminar Natural Convection Between Isothermal Vertical Parallel Plates with an Unheated Entry
Numerical Study of Natural Convection Between Two Vertical Parallel Plates with One Oscillating Surface Temperature
Author: Wei Cha
Publisher:
ISBN:
Category : Electronic apparatus and appliances
Languages : en
Pages : 196
Book Description
Publisher:
ISBN:
Category : Electronic apparatus and appliances
Languages : en
Pages : 196
Book Description
An Analysis of Natural Convection Between Finite Vertical Parallel Plates
Author: James Quintiere
Publisher:
ISBN:
Category : Fluid dynamics
Languages : en
Pages : 356
Book Description
Publisher:
ISBN:
Category : Fluid dynamics
Languages : en
Pages : 356
Book Description
Numerical Study of Transient Laminar Natural Convection Heat Transfer Over an Isothermal Sphere
Author: Shu Yang
Publisher:
ISBN:
Category :
Languages : en
Pages : 138
Book Description
Publisher:
ISBN:
Category :
Languages : en
Pages : 138
Book Description
Numerical Study of Asymmetric Natural Convection Between Vertical Isothermal Plates at Unequal Temperatures
Author: Doug Roberts
Publisher:
ISBN:
Category :
Languages : en
Pages :
Book Description
Publisher:
ISBN:
Category :
Languages : en
Pages :
Book Description
Applied Mechanics Reviews
Author:
Publisher:
ISBN:
Category : Mechanics, Applied
Languages : en
Pages : 620
Book Description
Publisher:
ISBN:
Category : Mechanics, Applied
Languages : en
Pages : 620
Book Description
Paper
Author:
Publisher:
ISBN:
Category : Mechanical engineering
Languages : en
Pages : 966
Book Description
Publisher:
ISBN:
Category : Mechanical engineering
Languages : en
Pages : 966
Book Description
Fully Developed Laminar Natural Convection in a Vertical Parallel Plate Channel with Symmetric Uniform Wall Temperature
Author: Robert H. Willie
Publisher:
ISBN:
Category : Heat
Languages : en
Pages : 72
Book Description
Described in this thesis is an investigation of the fully developed natural convection heat transfer in a vertical channel formed by two infinitely wide parallel plates maintained at a uniform wall temperature. Closed-form solutions for the velocity and temperature profiles are developed along with local and averaged Nusselt numbers. The local Nusselt number based on bulk temperature is found to be 3.77. This result is an analog corresponding to 7.60 for fully developed laminar forced convection in a parallel plate channel with uniform wall temperature boundary condition. The local Nusselt number based on the ambient temperature is deduced as a function of flowwise location. Results are compared with existing numerical and experimental data to find good agreement.
Publisher:
ISBN:
Category : Heat
Languages : en
Pages : 72
Book Description
Described in this thesis is an investigation of the fully developed natural convection heat transfer in a vertical channel formed by two infinitely wide parallel plates maintained at a uniform wall temperature. Closed-form solutions for the velocity and temperature profiles are developed along with local and averaged Nusselt numbers. The local Nusselt number based on bulk temperature is found to be 3.77. This result is an analog corresponding to 7.60 for fully developed laminar forced convection in a parallel plate channel with uniform wall temperature boundary condition. The local Nusselt number based on the ambient temperature is deduced as a function of flowwise location. Results are compared with existing numerical and experimental data to find good agreement.
Proceedings of the ASME Heat Transfer Division
Author:
Publisher:
ISBN:
Category : Combustion
Languages : en
Pages : 406
Book Description
Publisher:
ISBN:
Category : Combustion
Languages : en
Pages : 406
Book Description
Laminar Natural Convection Within Long Vertical Uniformly Heated Parallel-plate Channels and Circular Tubes
Author: Nat Vorayos
Publisher:
ISBN:
Category : Heat
Languages : en
Pages : 326
Book Description
The problem of simple mathematical models of laminar natural convective flow within a long vertical parallel-plate channels and circular tubes kept at uniformly heated walls is revisited to seek a clear physical understanding of heat transfer mechanisms. A series solution method to analyze the fully developed flow and an integral solution method to analyze the developing flow are used. Chapters 3, 4, and 5 of this dissertation constitute a series of three-paper manuscripts for submission to archival journals. The channels and circular tubes considered here are assumed to be sufficiently long to yield a fully developed flow thermally as well as hydrodynamically before the exit is encountered. In such fully developed flow situation, the fluid mass flow rate naturally induced into the channel due to buoyancy is found to be a function of the wall heating condition. The predicted average Nusselt number as a function of GrPrD/L not only agrees with the existing literature but also is found to be in a functional form comparable to that proposed by Elenbaas (1942 a and b). Our results show that, in spite of being driven by buoyancy (rather than by a pump or a blower), the flow and heat transfer characteristics in the fully developed regime are essentially the same as those of fully developed laminar forced convection in which the flow is externally driven. This observation is confirmed to be valid also in the study (Chapter 5) of laminar natural convection in the developing (entrance) region within a long vertical parallel-plate channel and circular tube. The mass flow rate, which has to remain invariant with axial location even in the entry region, is determined by the flow in the fully developed region. This is the same mechanism involved in forced convection in which the fluid outside the developing boundary layers (i.e. the core flow) is forced to accelerate in the entrance region. The entrance length of channel natural convection is also discovered to be about the same as that in forced convection.
Publisher:
ISBN:
Category : Heat
Languages : en
Pages : 326
Book Description
The problem of simple mathematical models of laminar natural convective flow within a long vertical parallel-plate channels and circular tubes kept at uniformly heated walls is revisited to seek a clear physical understanding of heat transfer mechanisms. A series solution method to analyze the fully developed flow and an integral solution method to analyze the developing flow are used. Chapters 3, 4, and 5 of this dissertation constitute a series of three-paper manuscripts for submission to archival journals. The channels and circular tubes considered here are assumed to be sufficiently long to yield a fully developed flow thermally as well as hydrodynamically before the exit is encountered. In such fully developed flow situation, the fluid mass flow rate naturally induced into the channel due to buoyancy is found to be a function of the wall heating condition. The predicted average Nusselt number as a function of GrPrD/L not only agrees with the existing literature but also is found to be in a functional form comparable to that proposed by Elenbaas (1942 a and b). Our results show that, in spite of being driven by buoyancy (rather than by a pump or a blower), the flow and heat transfer characteristics in the fully developed regime are essentially the same as those of fully developed laminar forced convection in which the flow is externally driven. This observation is confirmed to be valid also in the study (Chapter 5) of laminar natural convection in the developing (entrance) region within a long vertical parallel-plate channel and circular tube. The mass flow rate, which has to remain invariant with axial location even in the entry region, is determined by the flow in the fully developed region. This is the same mechanism involved in forced convection in which the fluid outside the developing boundary layers (i.e. the core flow) is forced to accelerate in the entrance region. The entrance length of channel natural convection is also discovered to be about the same as that in forced convection.