The partition of Europe, a textbook of European history, 1715-1815,

Mode of access: Internet.

Symphonie [no. 7] en sol mineur, pour grand orchestre. Op. 87. Partition.

Mode of access: Internet.

Time of concentration and storage coefficient values for Illinois streams /

Mode of access: Internet.

Rose et Colas opéra comique. Partition de piano et chant.

At head of cover: Bibliothéque de musique.

La partition de l'évêché de Térouane, 1559.

Mode of access: Internet.

Recherches sur l'organisation, la fructification et la classification de plusieurs genres d'algues : avec la description de quelques espèces inédites on peu connues : essai d'une répartition des polypiers calcifères de Lamouroux dans la classe des algues /

Spine title: Thése pour le doctorate.

Method of determining the coefficient of storage from straight-line plots without extrapolation /

Mode of access: Internet.

Investigations of evaporation from a screened pan and development of a coefficient for the conversion of pan evaporation to lake evaporation /

Mode of access: Internet.

Recherches sur les facteurs de la répartition et sur le role des mycorhizes,

At head of title: Faculté des Sciences de l'Université de Paris.

Cinq symphonies pour petit orchestre. Partition. 3. Sérénade (1921).

For flute, clarinet, bassoon, violin, viola, violoncello and double bass.

Recherches experimentales sur la dispersion rotatoire ; Etude numerique sur les relations entre le coefficient critique et le volume moleculaire /

Thesis (doctoral)--Universite de Geneve.

Contenancy and partition

Mode of access: Internet.

Hydrodynamics and mass transfer coefficient in activated sludge aerated stirred column reactor: Experimental analysis and modeling

The aerated stirred reactor (ASR) has been widely used in biochemical and wastewater treatment processes. The information describing how the activated sludge properties and operation conditions affect the hydrodynamics and mass transfer coefficient is missing in the literature. The aim of this study was to investigate the influence of flow regime, superficial gas velocity (U-G), power consumption unit (P/V-L), sludge loading, and apparent viscosity (pap) of activated sludge fluid on the mixing time (t(m)), gas hold-up (epsilon), and volumetric mass transfer coefficient (kLa) in an activated sludge aerated stirred column reactor (ASCR). The activated sludge fluid performed a non-Newtonian rheological behavior. The sludge loading significantly affected the fluid hydrodynamics and mass transfer. With an increase in the UG and P/V-L, the epsilon and k(L)a increased, and the t(m), decreased. The E, kLa, and tm,were influenced dramatically as the flow regime changed from homogeneous to heterogeneous patterns. The proposed mathematical models predicted the experimental results well under experimental conditions, indicating that the U-G, P/V-L, and mu(ap) had significant impact on the t(m) epsilon, and k(L)a. These models were able to give the tm, F, and kLa values with an error around +/- 8%, and always less than +/- 10%. (c) 2005 Wiley Periodicals, Inc.

Development of a non-intrusive heat transfer coefficient gauge and its application to high pressure die casting Effect of the process parameters

A heat transfer coefficient gauge has been built, obeying particular rules in order to ensure the relevance and accuracy of the collected information. The gauge body is made out of the same materials as the die casting die (H13). It is equipped with six thermocouples located at different depths in the body and with a sapphire light pipe. The light pipe is linked to an optic fibre, which is connected to a monochromatic pyrometer. Thermocouples and pyrometer measurements are recorded with a data logger. A high pressure die casting die was instrumented with one such gauge. A set of 150 castings was done and the data recorded. During the casting, some process parameters have been modified such as piston velocity, intensification pressure, delay before switch to the intensification stage, temperature of the alloy, etc.... The data was treated with an inverse method in order to transform temperature measurements into heat flux density and heat transfer coefficient plots. The piston velocity and the initial temperature of the die seem to be the process parameters that have the greatest influence on the heat transfer. (c) 2005 Elsevier B.V. All rights reserved.

Hydrodynamics and mass transfer coefficient in three-phase air-lift reactors containing activated sludge

This study was to investigate the impacts of operating conditions and liquid properties on the hydrodynamics and volumetric mass transfer coefficient in activated sludge air-lift reactors. Experiments were conducted in internal and external air-lift reactors. The activated sludge liquid displayed a non-Newtonian rheological behavior. With an increase in the superficial gas velocity, the liquid circulation velocity, gas holdup and mass transfer coefficient increased, and the gas residence time decreased. The liquid circulation velocity, gas holdup and the mass transfer coefficient decreased as the sludge loading increased. The flow regime in the activated sludge air-lift reactors had significant effect on the liquid circulation velocity and the gas holdup, but appeared to have little impact on the mass transfer coefficient. The experimental results in this study were best described by the empirical models, in which the reactor geometry, superficial gas velocity and/or power consumption unit, and solid and fluid properties were employed. (c) 2006 Elsevier B.V. All rights reserved.