Dynamic Model of Condensation in A Tube. by Atomic Energy of Canada Limited.

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SeriesAtomic Energy of Canada Limited. AECL -- 5603
ContributionsMcmorran, P.D., Moeck, E.O.
ID Numbers
Open LibraryOL21970771M

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The condensation heat transfer model proposed by Thome, El Hajal and Cavallini uses the same flow pattern map as for evaporation but with the new modifications noted above. The new condensation model assumes that two types of heat transfer occur around the perimeter of the tube: convective condensation and film condensation.

Abstract. The static condensation technique has been described extensively in the preceding chapter. Because the inertia effects are ignored in this condensation, the accuracy of the resulting reduced model is generally very low for dynamic problems.

The displacement, velocity and acceleration of Node 40 in horizontal direction (X direction) by the above three methods are displayed in Fig.

y, the curves obtained from the full model are nearly overlapped with those of the proposed condensed model, which implies that the proposed condensation method is accurate to calculate the structural responses of a by:   condensation of steam-air mixtures in a horizontal effects of inlet fluid temperature,air mass concentration and tube diameter on the rate of condensation were investigated.

It was found that condensation heat transfer coefficient drops by approximately 50% within an air mass of 3% and there after the drop in the heat transfer. flowing through the tube bundle. This zone is mod-elled by ‘Pipe 1’ in Figure 2. zone Four configurations of the model are possible (see Figure 2): 1.

horizontal water heater, with desuperheating zone, condensation zone and subcooled zone, 2. horizontal water heater, with condensation zone only, 3.

A dynamic condensation method using algebraic substructuring 2 September | International Journal for Numerical Methods in Engineering, Vol.

No. 12 Extending modal testing technology for model validation of engineering structures with sparse nonlinearities: A first case study. The proposed modification substantially reduces the number of numerical operations required in the application of the method and still provides accurate solutions for the higher modes of the system.

This modification is presented after a brief discussion of the static condensation method and a review of the original dynamic condensation method.

The condenser used to apply and validate the dynamic model is a shell-and-tube condenser (1–2) in which refrigerant is flow- ing through the shell and water inside the internal tubes. The condensation side is categorized by a thin laminar condensing layer (at the top of the tube), a stratified laminary layer (at the bottom of the tube), and a laminar or turbulent vapour zone.

In accordance with the model proposed by Fabbri, the steam condensation rate per unit of tube length is assumed constant along each tube: r x L M c T T m s air p i i s air i⋅ ⋅ ⋅ ⋅ − =+1.

In this demonstration, water liquid was heated to the boiling point till evaporation/condensation occurs. The evaporation/condensation model under the multip. The process of waste vapour condensation was studied inside the tubes of the vertical tube condenser, and the Dynamic Model of Condensation in A Tube.

book of the operation parameters and a comparison with the pure steam condensation. Pure component condensation with free convection can be described with the theory derived by Nusselt () for smooth tubes.

For low-finned tubes a wide range of experimental data is presented along with a newly developed model to predict the outer heat transfer coefficients.

The previous theoretical model of film condensation on a single horizontal low finned tube is extended to include the effect of condensate inundation. Based on the flow characteristics of condensate on a vertical column of horizontal low finned tubes, two major flow modes, the column mode and the sheet mode, are considered.

Condensation heat transfer for tube in bundle ranged from W/ m2K to 20, W/ m2K for the range of pressure studied. A heat and mass analogy model was developed and the condensation heat transfer prediction from the model was compared with experimental data. This video is about The Condensation Theory 1.

For the Love of Physics - Walter Lewin - - Duration: Lectures by Walter Lewin. To further improve the accuracy, in this article a new phase-change model is built using user-defined functions (UDFs).

The accuracy of this new phase-change model is verified by two evaporation problems (a one-dimensional Stefan problem and a two-dimensional film boiling problem) and one condensation problem (single steam bubble condensation.

dimensional condensation model using a k-E model for the turbulent vapor-air flow, the results of which were compared with the CVTR (Carolinas Virginia Tube Reactor) in- tegral test by using the vapor-air velocity predicted by a separate two-dimensional fluid dynamics model.

Investigations of steam condensation in a. The condensation process in horizontal tubes is much more complicated than in vertical tubes. Over the tube length different flow regimes (e.g. spray, plug, slug, bubble and stratified flow) may occur (see fig. Vapor enters the tube with a relatively high velocity and annular flow.

A typical example of condensation in a closed tube is a heat pipe. As shown in Figure 2 vapor generated in a heating section, i.e., an evaporator, flows into a condenser where the vapor condenses. The condensate returns to the evaporator as a liquid film on a tube wall.

Other methods have been developed for calculating the effects of steam condensation on the outer wall of a vertical tube in the presence of noncondensable gases.

For example, inresearchers [ 4 ] developed a steam condensation model for the outside of vertical tube geometries in the presence of noncondensable gases, such as air and helium. The key models for successful simulation appear to be the condensation model of the hot vapor on the cold liquid and the interfacial momentum transfer model.

The surface renewal types of condensation correlations, developed for condensation in the stratified flows, were used in the simulations and were applied also in the regions of the slug flow.

Rifert, V. G., et al.: Condensation inside Smooth Horizontal Tubes: Part 1. Survey of THERMAL SCIENCE, YearVol. 19, No. 5, pp. as many authors state) over tube perimeter and at a definite length (minimally m, but more often from m to m).

The thermal-hydraulic and physico-chemical code HELIOS is based on three-dimensional two-fluid model of steam, hydrogen and oxygen gas mixture and water condensate flow, as well as on the radiolytic gases mass conservation equations. Transport processes at the gas mixture-water condensate interface are modelled with appropriate closure laws.

where α 1, for the uppermost tube, is given by Eq.(2). In view of the more probable mode of drainage or inundation with condensate film disturbance due to splashing from droplets, columns or unstable broken films of liquid, it is not surprising that Eq.

(4) has been found to be overconservative. Many experimental studies of condensation on tube banks have been made. The main objective of this chapter is to study the liquid film condensation in a thermal desalination process, which is based on the phase change phenomenon.

The external tube wall is subjected to a constant temperature. The set of the non-linear and coupled equations expressing the conservation of mass, momentum and energy in the liquid and gas mixtures is solved numerically.

Rudy and Webb [10, 11] reported experimental investigations of condensate retention on three integral‐fin tubes and a spine‐fin tube with fin densities in a range of – fins per meter using n‐pentane, R‐11 and water under static (without condensation) and dynamic (with condensation) conditions.

For all the fluids, they found an. Based on the Nusselt model, the surface tension effect is not taken into account in the Beatty and Katz model, which plays an important role in condensation on a surface with fins.

The photographs taken during the experiments showed that the condensate dripping columns have a pitch is in agreement with that proposed by Yung et al. [24] for. Chapter 12 Liquids: Condensation, Evaporation, and Dynamic Equilibrium Changing from Gas to Liquid and from Liquid to Gas—An Introduction to Dynamic Equilibrium Our discussion of liquids focuses on two opposing processes: condensation, in which liquids are formed from gases, and evaporation, in which liquids return to gases.

The advent of large computer systems for structural analysis has sometimes led to the use of little-understood approximation techniques which can lead to undetected errors. For example, for dynamic analysis, only dynamic degrees of freedom at the points of significant mass and moment of inertia are.

able€to€model€two€phenomena:€the€condensation€rate€in€the€condenser,€and€the€flow€rate through€the€system.€This€report€concentrates€on€the€first€issue,€simulating€steam€condensation in€a€tube€in€the€presence€of€air,€with€MELCOR€€YV.€Experiments€that€were. The tube count depends on the factors like shell ID, OD of tube, tube pitch, tube layout, number of tube passes, type of heat exchanger and design pressure.

Tube passes The number of passes is chosen to get the required tube side fluid velocity to obtain greater heat transfer co-efficient and also to reduce scale formation.

by combination with the mechanistic CFD surface condensation model. Keywords: condensation, noncondensable gases, CFD simulation, boundary-layer approximation, binary and ternary mixtures. V List of papers and publications Publications and papers included I.

Karkoszka K., Anglart H., CFD modeling of laminar film and. phenomenological condensation model based on local flow patterns and interfacial wave effects for condensation inside plain tubes for a very wide range of parameters: mass velocities from 16 to Kg/m2s, tube internal diameters from to mm reduced pressure from to and vapor qualities from to analytical model is created using MATLAB (), while ANSYS Fluent (a) also requires water from a local source in order to perform condensation.

Plumes arevisible fromthedirect coolingsystem. A schematic ofthesystem canbeseen tive condensation in an inclined smooth tube, using Ra as their working fluid.

The simplest type of condenser is a straight tube, cooled only by the surrounding air. The tube is held in a vertical or oblique position, and the vapor is fed through the upper end.

The heat of condensation is carried away by convection. The neck of the retort is a classical example of a straight tube condenser. Condenser, device for reducing a gas or vapour to a sers are employed in power plants to condense exhaust steam from turbines and in refrigeration plants to condense refrigerant vapours, such as ammonia and fluorinated hydrocarbons.

The petroleum and chemical industries employ condensers for the condensation of hydrocarbons and other chemical vapours. leak in a tube wall or other connection will allow cooling water to be drawn into, and contaminate, the pure condensate. The present paper intends to present different modes of condenser tube leakages along with some case studies and possible remedial measures to prevent failure of condenser tubes Keywords: Crevice.

Please contact [email protected] or call (M – Th 9 am – pm and F 9 am – 3 pm. ET), to start a free trial, get pricing information, order a reprint, or post an. Shell and Tube Exchangers With shell and tube condensers, there is a choice between shell side or tube side condensation.

Tube side condensation is favored when the condensing fluid is at high pressure, is corrosive or prone to cause fouling. Shell side condensation is generally used for low pressures, and almost always for vacuum duties. Da Riva, E, & Del Col, D. "Numerical Simulation of Condensation in a Minichannel." Proceedings of the ASME Second International Conference on Micro/Nanoscale Heat and Mass Transfer.

ASME Second International Conference on Micro/Nanoscale Heat and Mass Transfer, Volume 2. Shanghai, China. December 18–21, pp. ASME.This is how condensation takes place, warm water vapor comes in contact with a surface that is colder than the surrounding area.

The cold ice water is the cold surface area that the warm water vapor comes in contact with causing it to change or condense. Connecting Evaporation and Condensation .A dynamic unconscious Freud was interested in a dynamic unconscious, made up of ideas that have been forced out of consciousness by a process of repression.

This is very different to ideas that are outside of consciousness but can become conscious quite easily – what Freud called the preconscious.

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