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New Jersey Institute of Technology

Heat -- Transmission

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Full-Text Articles in Engineering

A Study Of Heat Transfer And Inlet Flow Behavior In Molten Polymer Systems, Min Ho Choi May 1971

A Study Of Heat Transfer And Inlet Flow Behavior In Molten Polymer Systems, Min Ho Choi

Theses

Two separate studies have been done in the present work: one to study the entrance effects in flow in molten polymer systems and the other to investigate the heat transfer to thermally softened flowing polymer.

The equipment for the entrance effect was designed to study the isothermal flow behavior of a polymer melt in the entrance region. The main object of this investigation was to find the entrance length for the melt to relax and to separate the pressure drop into viscous and elastic effect. Due to the failure in developing a proper pressure measuring device the experiment was not …


The Relation Of Heat Transfer To Power Consumption Of Liquids In Turbulent Flow, John D. Bien Jun 1970

The Relation Of Heat Transfer To Power Consumption Of Liquids In Turbulent Flow, John D. Bien

Theses

The relationship between the heat transfer ability and the power input requirement of liquid coolants in a turbulent heat transfer condition was investigated. A correlation in terms of the liquid physical properties and the required volumetric flow was proposed and the use of this correlation in selection of liquids as coolant was discussed. The optimum condition for a high heat transfer/power input ratio was also discussed.


Batch Heat Transfer To Suspensions In An Agitated Vessel, John Philip Horzepa May 1970

Batch Heat Transfer To Suspensions In An Agitated Vessel, John Philip Horzepa

Theses

Batch heat transfer data was experimentally determined for two phase (solid?liquid) systems in a baffled agitated vessel. Three iron oxide and water and two kaolin and water suspensions were evaluated and were found to be pseudoplastic. A total of 231 heating and cooling data points were examined. Each suspension was evaluated using anchor, paddle, propeller and turbine impellers. Various sizes of the latter three impellers were used.

The experimental heat transfer results for suspensions were compared with the Hagedorn and Salamone correlation for pseudoplastic liquids. Only partial agreement with the more dilute suspensions was obtained. Overall, the data for suspensions …


Open-Loop Frequency Response Analysis Of A Jacketed Kettle With Internal Heating/Cooling Coil, Wayne P. Brenckle Jun 1967

Open-Loop Frequency Response Analysis Of A Jacketed Kettle With Internal Heating/Cooling Coil, Wayne P. Brenckle

Theses

This work was performed to investigate the response and stability of a jacketed kettle with internal heating/cooling coils and glasteel thermowell. This system was first analyzed mathematically by deriving transfer functions for each component and then combining all component equations together to give the overall system transfer function. The mathematical model was then checked by frequency response analysis of the system. Bode plots of the system were prepared and the effect of the thermowell was analyzed.

Nyquist plots of the system were used as the criteria for determining stability, and obtaining the open-loop gain necessary to give optimum closed-loop response. …


Heat And Mass Transfer In The Absence Of Air, James Joseph Howley Jun 1967

Heat And Mass Transfer In The Absence Of Air, James Joseph Howley

Theses

The effects of heat and mass transfer across a frosted heat exchanger operating in the absence of air was evaluated. It is felt that this work could be applied to processes such as desalination of water or the purification of materials by reverse sublimation.

The system consisted of a single 1/2” O.D. stainless steel tube mounted within a 3" O.D. plexiglas tube with the ends suitably flanged. A vacuum was maintained in the annular space. Refrigerated ethylene glycol passed through the inner tube in laminar flow. A series of runs with substantially air-free water vapor added to the annular space …


Heat Transfer Coefficients Of Non-Newtonian Slurries In Laminar Flow, Robert Frederick Roth, David B. Swanson Sep 1961

Heat Transfer Coefficients Of Non-Newtonian Slurries In Laminar Flow, Robert Frederick Roth, David B. Swanson

Theses

A total of 51 heat transfer runs were made in the first 25 runs, slurries of half micron and finer kaolin at 3.0, 5.6, 9.6 and 12.9% solids were used. Slurries of two microns and finer kaolin at 10.1, 13.7, 20.4 and 23.1% solids were used in the remaining 26 runs.

The Reynolds Numbers ranged from 0.9 to 2,020 for the 51 runs.

The data was correlated by the following equation:

Hf/CbVbPb CbRb/Kb 2/3 = 0.70 DVbPb/Rb -2/3

for an L/D ratio of …


Heat Transfer Coefficients Of Condensing Vapors, Charles Rocco Lipuma, Earl Adolph Nirmaier Jun 1956

Heat Transfer Coefficients Of Condensing Vapors, Charles Rocco Lipuma, Earl Adolph Nirmaier

Theses

The film coefficients of heat transfer for vapors condensing on a single horizontal tube have been measured for methyl, i-propyl, and n-butyl alcohols. The equipment used was specifically designed for these studies, and represents an improvement over that used by other investigators. The data collected were analyzed usingmodified Wilson method which is based on a rigorous theoretical analysis.

It has been found that the condensing film coefficients for methyl and i-propyl alcohols vary with the heat duty. This is to be expected from the analysis mentioned above. Me variation was found for n-butyl alcohol.

The observed values of the heat …


Heat Transfer Coefficients In An Agitated Vessel Using Verticle-Tube Baffles, Edward Joseph Barrasso Jun 1956

Heat Transfer Coefficients In An Agitated Vessel Using Verticle-Tube Baffles, Edward Joseph Barrasso

Theses

Data are presented to show the effect of impeller speed, impeller type, and fluid properties on the forced-convection film coefficient of heat transfer for verticle tubes in a cylindrical vessel. A generalized equation to predict the film coefficient of heat transfer on the outside of verticle tubes in an agitated vessel for both cooling and heating is also presented. This equation may be used to estimate the necessary areas of heat transfer for verticle tubes in an agitated vessel within the degree of accuracy required from most engineering calculations.

This study was the first initiated to develop an equation to …


The Analogy Between Heat And Mass Transfer In Packed Beds, Jasper Joseph Correnti Jun 1955

The Analogy Between Heat And Mass Transfer In Packed Beds, Jasper Joseph Correnti

Theses

An operation which recurs in many branches of chemical engineering is that in which a fluid - gas or liquid - is passed through a bed of granular solids for the purpose of removing from, or adding something to the fluid (or both). In the oil and sugar industries, oils or syrups are passed through beds of adsorbents to remove impurities causing color and other undesireable effects. In the recovery of volatile solvents, air charged with solvent vapor is passed over solid adsorbents. In leaching, liquids are passed through beds of solids to remove some constituent of the solids. In …


Jacket Heat Transfer Coefficients In An Agitated Vessel, The Paddle Agitator, Herbert Palfrey Pursell Jun 1954

Jacket Heat Transfer Coefficients In An Agitated Vessel, The Paddle Agitator, Herbert Palfrey Pursell

Theses

Four papers have been published which correlate variables affecting heat transfer through a jacket in a kettle agitated by a paddle type agitator. There are differences in the equations resulting from each of these papers. In none of these papers was variation of the stirrer diameter or stirrer width considered.

It is the purpose of this paper to show that all published data in such a system can be correlated by a single equation which differs from those previously presented. Preliminary recalculation of published data indicated that a relationship exists which involves the stirrer width and diameter. Experimental work was …


Heat Transfer Characteristics Of Non-Newtonian Suspensions, Harold Binder May 1954

Heat Transfer Characteristics Of Non-Newtonian Suspensions, Harold Binder

Theses

The following equation was developed by Dr. J. J. Salamone for calculating the fibs coefficient of heat transfer to non-Newtonian suspensions in turbulent flow (Re 50,000 - 200.000) inside of pipes:

hD/Kf = 0.131 (DVbPb/ub)0.62 (D/Ds)0.05 (Cs/Cf)0.35 (Cfub/Kf)0.72 (Ks/Kf)0.05

This equation was investigated to determine its validity over the lower turbulent regions of the Reynolds number (10,000 - 70,000), and to test the exponents of the various components.

Equipment was constructed similar …