2 edition of **Laminar-pseudoplastic-flow heat transfer in the entrance region of a tube.** found in the catalog.

Laminar-pseudoplastic-flow heat transfer in the entrance region of a tube.

G. Forrest

- 170 Want to read
- 8 Currently reading

Published
**1969**
in Bradford
.

Written in English

**Edition Notes**

M Sc. dissertation. Typescript.

Series | Dissertations |

The Physical Object | |
---|---|

Pagination | 24p. |

Number of Pages | 24 |

ID Numbers | |

Open Library | OL13688412M |

Leonhardt, W. J. and Irvine, T. F. Jr. () Experimental friction factors for fully developed flow of dilute aqueous polyethylene-oxide solutions in smooth wall triangular ducts, Heat and Mass Transfer Source Book (Fifth All-Union Conference, Minsk), , Scripta Publishing Co. and John Wiley and Sons. Heat Exchangers 73 individual thermal resistances of the system. Combining each of these resistances in series gives: 1 UA = 1 (ηohA)i 1 Skw 1 (ηohA)o () where η0 is the surface eﬃciency of inner and outer surfaces, h is the heat transfer coeﬃcients for the inner and .

Turbulent heat transfer to CO 2 at supercritical pressure flowing in heated vertical tubes is investigated using direct numerical simulation at the inlet Reynolds number Re 0 = , which is based on inlet bulk velocity and tube ature range within the flow field covers the pseudocritical region, where very significant fluid property variations are involved. TECH LIBRARY KAFB, NM 1. Report No. I 2. Government Accession No. I 3. Recipient's NASA TN D 1 4. Title and Subtitle Date ANALYSIS OF DEVELOPING LAMINAR FLOW AND HEAT TRANSFER IN A TUBE FOR A GAS WITH COOLING 6. Performing Organization Code.

Book Search tips Selecting this option will search all publications across the Scitation platform Selecting this option will search all publications for the Publisher/Society in context. Entrance region heat transfer with axial conduction in a cylindrical tube: Constant wall heat flux The Physics of Flu ( Answer: Heat Transfer rate is better in a Turbulent Flow. (If you want to understand why, then delve further into the answer) Reason: Laminar and Turbulent Flow regimes in cigarette smoke The flow regime near the cigarette butt is said to be Lamin.

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Laminar Flow Heat Transfer in Tubes 1 Literature Survey 2 Laminar Flow Heat Transfer Augmentation in Tubes 8 Scope of Investigation 16 CHAPTER II. ANALYTICAL SOLUTIONS FOR COMBINED FORCED AND FREE LAMINAR CONVECTION IN THE ENTRANCE REGION OF HORIZONTAL TUBES 18 Introduction 18 Formulation of the Problem 23Cited by: 4.

However, the complete solution to this problem, in terms of engineering usage, also requires the determination of one or more of the following: (1) local and mean wall heat fluxes, (2) local and mean Nusselt numbers, (3) the thermal entrance length, (4) incremental heat transfer rate in the entrance region over and above the fully developed.

Satish G. Kandlikar, in Heat Transfer and Fluid Flow in Minichannels and Microchannels (Second Edition), Fully developed laminar flow.

The Nusselt number in fully developed laminar flow is expected to be constant, as predicted by classical theory. However, there are a number of investigations reported in the literature that show a trend increasing with the Reynolds number in this. FOR the purpose of heat-exchanger calculations for deep hypothermia, the cooling of the blood flowing through a horizontal tube and annulus, with Reynolds number in Cited by: 6.

Simultaneously developing three-dimensional laminar flow and heat transfer in the entrance region of trapezoidal channels have been investigated using numerical methods in the Reynolds number range from 10 to Cited by: Analysis of laminar flow forced convection heat transfer with uniform heating in the entrance region of a circular tube.

The Canadian Journal of Chemical Engineering, Vol. 70, Issue. 6, p. The Canadian Journal of Chemical Engineering, Vol. 70, Issue. 6, p. Simultaneously developing laminar ow and heat transfer in the entrance region of at and circular conduits. Ph.D. thesis, Colorado School of Mines, Golden, CO.

Bogue, D. Correlations for Laminar Forced Convection in Flow Over an Isothermal Flat Plate and in Developing and Fully Developed Flow in an Iso- Thermal Tube.

(2) Heat transfer coefficient (3) Surface temperature Hydrodynamic and Thermal Regions: General Features x Fluid enters with uniform velocity and temperature. (1) Entrance region. Extends from the inlet to the section where the boundary layer thickness reaches the center of channel.

(2) Fully developed region. This zone follows the entrance. This paper describes the results of an experimental investigation into the velocity and turbulence fields and to a lesser extent the heat transfer in the entrance regions of short, circular cross-section pipes with length to diameter ratios up to 20 over the Reynolds number range f toWe use cookies to offer you a better experience, personalize content, tailor advertising, provide social media features, and better understand the use of our services.

A good design of a heat exchanger should consider methods of increasing heat transfer performance whilst reducing the pressure drop [1].

It is accepted in literature that the transition from laminar to turbulent flow occurs at a Reynolds number of [2]. Turbulent flow provides the best heat transfer coefficients with the disadvantage of. By experimentation, it has been found that Reynolds numbers of less than describe the condition at which there is no breaking away from the tube wall which is termed laminar flow.

The physical properties of the fluid are the determining factors for the heat transfer in this area which is inefficient in heat transfer. In heat transfer, as the fluid flows along the tube, the wall layers are heated or cooled.

In this case, at the entrance region of the tube, the fluid core retains a temperature equal to that at the inlet T 0 and does not participate in heat transfer. Temperature variation occurs in the wall layers. Mean temperature variation along a tube We are still left with the problem of knowing how the mean temperature T m(x), varies as a function of distance, so that we can use it in Newton’s law of cooling to estimate convection heat transfer.

Ø Consider an energy balance on a differential control volume inside the tube: dq conv = m. c p dT m. 1/25/Heat Transfer 14 The friction factor and the heat transfer coefficient are highest at the tube inlet where the thickness of the boundary layers is zero, and decrease gradually to the fully developed values, as shown in Fig.

Therefore, the Pressure drop and heat flux are higher in the entrance regions of a tube, and the effect of the. An analysis has been performed using a method similar to Graetz’s formulation for the laminar thermal entry region.

The fluid is assumed to have a fully developed turbulent velocity profile throughout the length of the pipe. Local and fully developed Nusselt numbers are presented for fluids with Prandtl numbers ranging from to for Reynolds numbers between and @article{osti_, title = {Simultaneously developing, laminar flow, forced convection in the entrance region of parallel plates}, author = {Nguyen, T V and Maclain-cross, I L}, abstractNote = {This paper reports on a numerical study of simultaneously developing flow in the entrance region of a cascade of thin parallel horizontal plates with a uniform flow at upstream infinity.

Parakash C, Liu YD () Analysis of laminar flow and heat transfer in the entrance region of an internally finned circular duct. J Heat Transfer –91 CrossRef Google Scholar Heat Transfer Engineering Thermodynamics Engineering Physics.

Forced Convection Entry Region Circular Pipe / Tube Equation and Calculator. Equation and calculator to determine the mean heat transfer coefficient for simultaneously developing velocity and temperature fields in a circular smooth tube. ALL calculators require a Premium Membership.

Hydrodynamic and thermal characteristics of Al 2 O 3 – water nanofluid flow at entry region of a uniformly heated pipe are studied applying finite control volume method (FCV).

Single phase and Eulerian-Eulerian two-phase models were used in modelling of nanofluid flow and heat transfer.In laminar flow in a tube with constant surface temperature, both the friction factor and the heat transfer coefficient remain constant in the fully developed region.

Constant Surface Heat Flux. Therefore, for fully developed laminar flow in a circular tube subjected to constant surface heat flux, the Nusselt number is a.Heat Transfer Coefficients. The evaluation of the overall heat transfer coefficient is an important part of the thermal design and analysis of a heat exchanger.

You’ll find several tables of typical overall heat transfer coefficients in shell-and-tube heat exchangers in Chapter 11 of Perry’s Handbook. The following.