2 edition of **Laminar heat transfer and power input in agitated vessels.** found in the catalog.

Laminar heat transfer and power input in agitated vessels.

Salah Eddine Ghenai

- 90 Want to read
- 17 Currently reading

Published
**1980**
in Bradford
.

Written in English

**Edition Notes**

M.Sc. dissertation. Typescript.

Series | Dissertations |

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

Pagination | 133p. |

Number of Pages | 133 |

ID Numbers | |

Open Library | OL13784474M |

With respect to oxygen transfer rates in air-liquid agitated systems, if the air rate is kept constant, the mass-transfer coefficient increases when power input to the impeller is increased. In terms of primary operating variables, an increase of impeller speed or impeller diameter will increase the rate of mass transfer a t a given air rate. 4. Agitation of the fluid to increase heat transfer between the fluid and a coil or jacket in the vessel wall. 5. Suspension of fine solid particles in a liquid, such as in the catalytic hydrogenation of a liquid where solid catalyst and hydrogen bubbles are dispersed in the liquid. Kurdistan Technical Institute - PD Dept. 5 Introduction: Agitator.

Polkowski, Janusz W. "An Influence of the Thickness of a Laminar Sublayer and Mixing Length Model on the Skin Friction and Heat Transfer in the Boundary Layer Flow." Proceedings of the ASME International Gas Turbine Conference and Exhibition. Volume 1: Turbomachinery. Anaheim, California, USA. May 31–June 4, VT01A ASME. the heat transfer rates. Because heat transfer in agitated vessels is complex, an empirical approach based on dimensionless analysis has been used to predict the average heat transfer coefficients at the jacketed wall. Hence, the results of many heat transfer studies are frequently correlated using a dimensionless equation. 0 Q L à 5 4.

Two types of heat-transfer boundary conditions are considered: (a) The channel walls are at constant temperature; or (b) a specified uniform heat flux is transferred at the walls. The heat-transfer behavior is obtained along the entire length of the channel, that is, in both the . Volumetric mass transfer coefficient, power input and gas hold-up in viscous liquid in mechanically agitated fermenters. Measurements and scale-up. International Journal of Heat and Mass Transfer , , DOI: /masstransfer

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(21) Most of the experimental data for heal transfer in agitated non-Newtonian liquids were interpreted simply by using the fictitious value according to the formula Papp = K(ANy instead of viscosity, usually having the same value (k = il) as suggested by Metzner and Otto () for correlation of power input in a laminar by: For laminar flow heat transfer •Determination of the overall heat transfer coefficient using logarithmic mean temperature difference •Calculation for the individual film heat transfer coefficient •Verification of Sieder-Tate equation.

Principle. Background Theory With respect to the inside area. The project on heat transfer surfaces in agitated vessels is based on the determination of the heat exchange area, which is necessary to abide by the process conditions as mixing quality and efficiency of heat transfer.

The heat transfer area is determined from the overall heat transfer coefficient (U). The coefficient (U) represents the operation quality in heat transfers being a function of. Flow Dynamics, Heat and Mass Transfer in Two-Phase Laminar and Turbulent Boundary Layer on a Flat Plate with and without Heat Transfer Between Solid Wall and Flow: The State-of-the-Art.

Pages Terekhov, Viktor I. (et al.). The project on heat transfer surfaces in agitated vessels is based on the determination of the heat exchange area, which is necessary to abide by the process conditions as mixing quality and. Heat transfer to Newtonian (water) and power law Non-Newtonian (1%, 2% and 4% aqueous CMC solution) fluids in the agitated vessel is investigated.

The data have been obtained for fluid agitated by three marine agitators ofand cm diameter respectively. The heat transfer coefficient has been calculated using Wilson graphical method with modification suggested by Om Prakash et al.

Arial Calibri Franklin Gothic Medium Cond Times New Roman Symbol Mountain Top 1_Mountain Top HEAT TRANSFER IN AGITATED VESSELS HEAT TRANSFER IN AGITATED VESSELS – A free PowerPoint PPT presentation (displayed as a Flash slide show) on. Comparing Heat Transfer Predictions for Jacketed Vessels The values of the constant k in the heat transfer equation (1) for the various impellers along with the power number P.

Mohan et al. Table 4 Vessel 1 Vessel 2 A. Test Vessels Diameter of the vessel, Dr m m Height of the liquid in the vessel, HL m m Height of the Cited by: An Equation for Laminar Flow Heat Transfer for Constant Heat Flux Boundary Condition in Ducts of Arbitrary Cross-Sectional Area J.

Heat Transfer (August, ) Forced Convection Heat Transfer From a Low-Profile Block Simulating a Package of Electronic EquipmentCited by: Power characteristics for an agitated vessel equipped with planar short baffles of length L and pitched blade turbine of pitch β are presented in the paper.

The studies were carried out in the vessel of inner diameter D = m, where the baffles were located in the distance p from the vessel bottom (p + L = H). Torque was measured using strain gauge method within the turbulent regime of Cited by: 3. Heat transfer rates in agitated vessels has been investigated for some Newtonian and non-Newtonian fluids mixed in a flat bottomed vessel equipped with a helical ribbon agitator.

Introductory heat transfer books are devoted primarily to the study of the basic rate phenomena of conduction, convection, and radiation, showing how to evaluate “h,” “U,” and “k” for this and that geometry and situation. Again, this book’s approach is different. We rapidly summarize the basic equations of heat transfer.

Over-all Heat Transfer Coefficients in Agitated Vessels _____ exchange, R. A, is the reciprocal of the product terms area, A. A, and heat transfer coefficient, h. Expressed mathematically, the temperature driving force is: ΔT.

A = (T. WA – T. A) (1) and the resistance equation across the hot fluid is: RFile Size: KB. Agitated vessel heat transfer is commonly used in batch manufacture where it is frequently necessary to calculate the time to heat or cool a batch or the cooling capacity required to hold an exothermic or endothermic reaction at constant temperature.

@article{osti_, title = {HEAT TRANSFER WITH LAMINAR FLOW IN CONCENTRIC ANNULI WITH CONSTANT AND ARBITRARY VARIABLE AXIAL WALL TEMPERATURE}, author = {Viskanta, R.}, abstractNote = {An analysis has been performed to determine the heat transfer characteristics for laminar forced-convection flow in a concentric annulus with prescribed surface temperatures.

Mechanical Agitator Power Requirements for Liquid Batches Instructor: John Frank Pietranski, P.E., Ph.D. liquids, such as methyl alcohol and water. The second is to promote heat transfer between the batch liquid and a coil or jacket.

T = diameter of the vessel or tank. The power input to a frictionless impeller is derived in detail. Ragunathan, Srivathsan, and Goering, Douglas J. "Numerical Analysis of Heat Transfer in a Laminar, Submerged, Slot Jet Impinging on an Oscillating Wall." Proceedings of the ASME Heat Transfer Summer Conference collocated with the ASME 13th International Conference on Author: Srivathsan Ragunathan, Douglas J.

Goering. Turbulent flow provides the best heat transfer coefficients with the disadvantage of high pressure drops, whereas the opposite is true for laminar flow.

The alternative is to consider transitional flow, which would provide better heat transfer characteristics than laminar flow with. Heat transfer rates in agitated vessels are very important for many applications, and there are many papers and studies on heat transfer in mixing vessels [1].

Many studies and analyzes of. The concepts of fully developed flow and heat transfer have been generalized to accommodate ducts whose cross-sectional area varies periodically in the streamwise direction.

The identification of the periodicity characteristics of the velocity components and of a reduced pressure function enables the flow field analysis to be confined to a. Let’s consider the governing equations.

Heat transfer through the vessel wall is governed by the generic equation: where N Nu is the Nusselt number, K is a heat-transfer constant, N Pr is the Prandtl number, and N Re is the Reynolds number. The constant K depends on impeller type and includes geometric factors such as impeller-to-tank-diameter ratio, pitch, diameter, etc.The unsteady, laminar, free-convection boundary layer is analyzed with the Grashof number considered to be time-dependent through either the uniform wall temperature or the acceleration field.

Two geometries are considered; the vertical plate and the horizontal circular by: 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.