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Compressibility bulk density

Powder properties for compression Bulk density 0.35 g/mL, tapped density 0.48, average particle size 122 pm. [Pg.996]

Different commonly used compression characterization methods have been demonstrated the Brazilian test, the confined uniaxial and unconfined compression test, and the flexible boundary cubical triaxial test. The HHP method appears as a new and promising possibility within the traditional compression methods. In HHP, higher pressure gives higher bulk density however, beyond a critical given pressure, the final compressed bulk density remains constant (ultimate bulk density). Further studies will determine whether this concept can be included as a quality descriptor in the specification data sheets of commercial food agglomerates. [Pg.300]

Compressibility. The bulk density of a soHd is an essential value used in the analysis of its flow properties, such as when calculating mass flow hopper angles, opening sizes, bin loads, etc. Loose and/or packed density values ate not sufficient. Bulk soHds exhibit a range of densities that vary as a function of consoHdating pressure. This range of densities, called the compressibiHty of the soHd, can often be expressed on a log—log plot as a line or relationship. [Pg.554]

The foUowing variables can affect a material s bulk density. (/) Moisture higher moisture content often makes a material mote compressible. (2) Particle size and shape often, the finer the bulk soHd, the mote compressible it is. The shape of the particles can affect how they fit together and thein tendency to break while being compacted. (3) Temperature some materials become mote compressible as thein temperature increases. This could be due, for example, to softening of the particles. (4) Particle elasticity elastic materials tend to deform significantly when they ate compressed. [Pg.554]

Other Fiber Evaluation Methods. The extent of fiber separation (fiber openness) is an important evaluation criteria that is commonly measured by several techniques, namely ak permeabiUty, adsorbed gas volume, bulk density, and residence (compression and recovery). The adsorption and retention of kerosene is also used as a measure of fiber openness and fiber adsorption capacity (34). [Pg.353]

Stmcture is usually measured by a void volume test such as the absorption of dibutyl phthalate (DBPA) (15), or by bulk density measurements of the carbon black under compression. In order to eliminate the effects of pelletizing conditions the DBPA test has been modified to use a sample that has been precompressed at a pressure of 165 MPa (24,000 psi) and then broken up four successive times (24M4) (16). This procedure causes some aggregate breakdown and is claimed to more closely approximate the actual breakdown that occurs duting mbber mixing. [Pg.542]

Filter aids should have low bulk density to minimize settling and aid good distribution on a filter-medium surface that may not be horizontal. They should also be porous and capable of forming a porous cake to minimize flow resistance, and they must be chemically inert to the filtrate. These characteristics are all found in the two most popular commercial filter aids diatomaceous silica (also called diatomite, or diatomaceous earth), which is an almost pure silica prepared from deposits of diatom skeletons and expanded perhte, particles of puffed lava that are principally aluminum alkali siheate. Cellulosic fibers (ground wood pulp) are sometimes used when siliceous materials cannot be used but are much more compressible. The use of other less effective aids (e.g., carbon and gypsum) may be justified in special cases. Sometimes a combination or carbon and diatomaceous silica permits adsorption in addition to filter-aid performance. Various other materials, such as salt, fine sand, starch, and precipitated calcium carbonate, are employed in specific industries where they represent either waste material or inexpensive alternatives to conventional filter aids. [Pg.1708]

In the 1990s this approach became more common in order to ensure sufficient compressive strength with the trend to lower bulk densities. Furthermore the proportion of SAN to polyol has been increased to about 40%. This may lead to serious stability problems and care must be taken to control the size and distribution of the particles and prevent agglomeration. Polymer polyols using polystyrene as the polymer component have recently become available (Postech-Shell) and are claimed to exhibit good stability, low viscosity and less discolouration as well as providing price advantages. [Pg.796]

Compressibility Disposal Abitrary methods relating changes in bulk density ASTM methods... [Pg.540]

A MC study of adsorption of living polymers [28] at hard walls has been carried out in a grand canonical ensemble for semiflexible o- 0 polymer chains and adsorbing interaction e < 0 at the walls of a box of size C. A number of thermodynamic quantities, such as internal energy (per lattice site) U, bulk density (f), surface coverage (the fraction of the wall that is directly covered with segments) 9, specific heat C = C /[k T ]) U ) — U) ), bulk isothermal compressibility... [Pg.532]

The bulk density of a powder is calculated by dividing its mass by the volume occupied by the powder (Abdullah Geldart, 1999). Tapped bulk density, or simply tapped density, is the maximum packing density of a powder achieved under the influence of well-defined, externally applied forces (Oliveira et al., 2010). Because the volume includes the spaces between particles as well as the envelope volumes of the particles themselves, the bulk and tapped density of a powder are highly dependent on how the particles are packed. This fact is related to the morphology of its particles and such parameters are able to predict the powder flow properties and its compressibility. [Pg.67]

With traditional solvents, the solvent power of a fluid phase is often related to its polarity. Compressed C02 has a fairly low dielectric constant under all conditions (e = 1.2-1.6), but this measure has increasingly been shown to be insufficiently accurate to define solvent effects in many cases [13], Based on this value however, there is a widespread (yet incorrect ) belief that scC02 behaves just like hexane . The Hildebrand solubility parameter (5) of C02 has been determined as a function of pressure, as demonstrated in Figure 8.3. It has been found that the solvent properties of a supercritical fluid depend most importantly on its bulk density, which depends in turn on the pressure and temperature. In general higher density of the SCF corresponds to stronger solvation power, whereas lower density results in a weaker solvent. [Pg.218]

The compressibility of a material can be estimated from the tap and bulk density measurements [69] ... [Pg.276]

Porosity calculations from density measurements have also been applied to granulations prepared using different processes. The method of granulation, such as the type of adjuvant used [64] or the amount of granulation liquid [74], was found to change the bulk density and porosity of the material. Consequently, the compression and flow properties of the materials were also different. [Pg.277]

In recent years the compressibility index Ci( has become a simple, fast, and popular method of predicting powder flow characteristics [40,42-44,51,52]. Carr [42-44] proposed its use as an indirect measure of bulk density, size and shape,... [Pg.294]

Product Name Thickness (mm) Weight (g/m ) Bulk Density (g/cm ) Porosity (%) Tensile Strength (MPa) Stiffness (Taber) Through-Plane Air Permeability (sec/100 cc) In-Plane Air Permeability (sec/100 cc) Compressibility (%) Through- Plane Resistivity (mohm cm ) In-Plane Resistivity (mohm cm) Comments ... [Pg.198]

Product Thickness Weight Bulk Density Porosity Tensile Strength Stiffness Through-Plane Air Permeability In-Plane Air Permeability Compressibility Through- plane Resistivity In-Plane Resistivity... [Pg.200]

As shown in Fig. 4.1, resin feedstocks have a considerable level of interparticle space that is occupied by air. This level of space and thus the bulk density of the feedstock depend on the temperature, pressure, pellet (or powder) shape, resin type, and the level and shape of the recycle material. For a specific resin feedstock, the bulk density Increases with both temperature and the applied pressure. Understanding the compaction behavior of a resin feedstock is essential for both screw design and numerical simulation of the solids-conveying and melting processes. Screw channels must be able to accommodate the change in the bulk density to mitigate the entrainment of air and the decomposition of resin at the root of the screw. Typically, screw channels are set by using an acceptable compression ratio and compression rate for the resin. These parameters will be discussed in Section 6.1. [Pg.112]

The plastic flow of sulfur is thought to be responsible for the increase in the burning time that is experienced with black powders of various pellet sizes as the pellets (or grains) are compressed to higher bulk densities. [Pg.24]


See other pages where Compressibility bulk density is mentioned: [Pg.3283]    [Pg.252]    [Pg.3283]    [Pg.252]    [Pg.524]    [Pg.547]    [Pg.549]    [Pg.208]    [Pg.471]    [Pg.1708]    [Pg.1891]    [Pg.1969]    [Pg.215]    [Pg.351]    [Pg.372]    [Pg.114]    [Pg.134]    [Pg.120]    [Pg.121]    [Pg.359]    [Pg.191]    [Pg.192]    [Pg.399]    [Pg.404]    [Pg.410]    [Pg.414]    [Pg.577]    [Pg.612]    [Pg.99]    [Pg.249]    [Pg.486]   
See also in sourсe #XX -- [ Pg.93 ]




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