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Upper converted

In [91], Chen studies the long wave asymptotics of the concentric Poiseuille flow of two upper-converted Maxwell fluids under axisymmetric perturbations. He concludes that stability can generally be achieved by increasing the volume of the more elastic component , in agreement with the lubrication effect. The corresponding short wave asymptotic study of the same flow is done in [92]. In the case of coextrusion flows a study for arbitrary wavelengths and low Reynolds numbers is done in [93]. [Pg.224]

Here, C denotes the configuration tensor and D describes the rate-of-strain tensor of the material continuum. The dimensionless anisotropy factor, cc, characterizes the anisotropic character of the particle mobility. It is easy to show that a attains values between zero and one. The limiting case a = 0 corresponds to the isotropic motion and ultimately leads to an upper converted Maxwell material. In order to derive a deformation-dependent constitutive equation, a Hookean law connecting the tensor of external stresses S, the configuration tensor C, and the shear modulus G was suggested ... [Pg.445]

Numerical simulation of the fiber-spinning process began with the early work of Matovich and Pearson [92], who analyzed the spinning of a Newtonian liquid and arrived at an analytical solution. Attempts were then made to analyze the process with differential constitutive models. Early work by Denn et al. [93] considered the upper converted Maxwell model, including nonisothermal effects [94]. Later, Gagon and Denn [95] used the PTT model and included nonisothermal effects to simulate... [Pg.164]

This constitutive equation is referred to as the upper converted Maxwell (UCM) model. In Example 3.1 this time derivative will be written out for simple shear and shear-free flows. The predictions of this model for steady shear... [Pg.45]

Block 2 A/D converter, has a filter of upper frequencies, speed conveyor A/D and buffer memory. Maximum frequency of transformation is 320 MHz. [Pg.731]

Convert the upper curve of Fig. XVII-31a to an adsorption isotherm, that is, to a plot of V versus P/I. ... [Pg.675]

We can now proceed to the generation of conformations. First, random values are assigne to all the interatomic distances between the upper and lower bounds to give a trial distam matrix. This distance matrix is now subjected to a process called embedding, in which tl distance space representation of the conformation is converted to a set of atomic Cartesic coordinates by performing a series of matrix operations. We calculate the metric matrix, each of whose elements (i, j) is equal to the scalar product of the vectors from the orig to atoms i and j ... [Pg.485]

Let us suppose that we can convert the n x coefficient matrix in equation system (6.5) into an upper triangular form as... [Pg.200]

Many pairs of partially miscible liquids possess neither a lower nor an upper C.S.T. for reasons outlined in the previous paragraph. Thus consider the two liquid phases from the two components water and diethyl ether. Upon cooling the system at constant pressure, a point will be reached when a third phase, ice, will form, thus rendering the production of a lower C.S.T. impossible, likewise, if the temperature of the two layers is raised, the critical point for the ether rich layer will be reached while the two liquid phases have different compositions. Above the critical point the ether-rich layer will be converted into vapour, and hence the system will be convert into a water rich liquid and an ether rich vapour the upper C.S.T. cannot therefore be attained. [Pg.19]

Hydrolysis (or saponification) of n-butyl acetate. Boil 4-5 g. of n-butyl acetate (Section 111,95) with 50 ml. of 10 per cent, sodium hydroxide solution under reflux until the odour of the ester can no longer be detected (about 1 hour). Set the condenser for downward distiUation and coUect the first 10 ml. of distillate. Saturate it with potassium carbonate, aUow to stand for 5 minutes, and withdraw all the Uquid into a small pipette or dropper pipette. AUow the lower layer of carbonate solution to run slowly into a test-tube, and place the upper layer into a small test-tube or weighing bottle. Dry the alcohol with about one quarter of its buUr of anhydrous potassium carbonate. Remove the alcohol with a dropper pipette and divide it into two parts use one portion for the determination of the b.p. by the Siwoloboff method (Section 11,12) and convert the other portion into the 3 5-dinitrobenzoate (Section III, 27) and determine the m.p. [Pg.390]

As cosmic rays pass through the upper atmosphere, some of the present is converted to by the capture of high-energy neutrons. The then migrates into... [Pg.647]

The largest consumer of coke is the iron and steel industry. In the United States, ca 600 kg of coke is used to produce a metric ton of steel. Japanese equipment and practice reduce the requirement to 400—450 kg. Coke is also used to gas from the char in one vessel. The reducing gas converts iron oxide to iron in the upper two stages of a second vessel. Steam is converted to hydrogen and reoxidizes the iron in two stages in the lower half of the vessel. [Pg.234]

The catalyst temperature is about 1100°C. Precious metal catalysts (90% Pt/10% Rh in gauze form) are normally used in the commercial processes. The converters are similar to the ammonia oxidation converters used in the production of nitric acid (qv) although the latter operate at somewhat lower temperatures. The feed gases to the converter are thoroughly premixed. The optimum operating mixture of feed gas is above the upper flammabiUty limit and caution must be exercised to keep the mixture from entering the explosive range. [Pg.377]

The solution is started by using Eq. (13-25) to convert the external-reflnx ratio of 4.5 to an internal-reflnx ratio of L/V = 0.818. The Xo = 0.95 value is then located on the diagonal, and the upper operating line is drawn as shown in Fig. 13-35. [Pg.1269]

FIG. 14-49 Pressure drop/flooding correlation of Kister and GiU for 2-inch metal Pali rings. The upper chart is for nonaqueous systems, the lower chart for aqueous systems. To convert inches H20/ft to mm H20/m, multiply by 83.31. [Pg.1390]

In making the edge dislocation of Fig. 9.3 we could, after making the cut, have displaced the lower part of the crystal under the upper part in a direction parallel to the bottom of the cut, instead of normal to it. Figure 9.7 shows the result it, too, is a dislocation, called a screw dislocation (because it converts the planes of atoms into a helical surface, or screw). Like an edge dislocation, it produces plastic strain when it... [Pg.99]

In the basic metric matrix implementation of the distance constraint technique [16] one starts by generating a distance bounds matrix. This is an A X y square matrix (N the number of atoms) in which the upper bounds occupy the upper diagonal and the lower bounds are placed in the lower diagonal. The matrix is Ailed by information based on the bond structure, experimental data, or a hypothesis. After smoothing the distance bounds matrix, a new distance matrix is generated by random selection of distances between the bounds. The distance matrix is converted back into a 3D confonnation after the distance matrix has been converted into a metric matrix and diagonalized. A new distance matrix... [Pg.75]

A molecular dynamics force field is a convenient compilation of these data (see Chapter 2). The data may be used in a much simplified fonn (e.g., in the case of metric matrix distance geometry, all data are converted into lower and upper bounds on interatomic distances, which all have the same weight). Similar to the use of energy parameters in X-ray crystallography, the parameters need not reflect the dynamic behavior of the molecule. The force constants are chosen to avoid distortions of the molecule when experimental restraints are applied. Thus, the force constants on bond angle and planarity are a factor of 10-100 higher than in standard molecular dynamics force fields. Likewise, a detailed description of electrostatic and van der Waals interactions is not necessary and may not even be beneficial in calculating NMR strucmres. [Pg.257]

The objective of combining two power plants in this way is to obtain greater work output for a given supply of heat or fuel energy. This is achieved by converting some of the heat rejected by the upper plant into extra work in the lower plant. [Pg.3]

The effect of the temperature on the polymerization of 53 in methylene chloride is presented in Table 3. The upper half of the data in the table shows the temperature effect on the products in the initial stage of the reaction, and the lower half is that for the middle to final stages of the reaction. Obviously there is a drastic change in the reaction products between -20 and -30 ° Below —30 °C, the cyclic dimer is the predominant or even sole product after the reaction of 48 hours, while above —20 °C, the low molecular weight polymer is exclusively formed. The cyclic oligomers once formed in the initial stage of the reaction are converted to the polymer in the later stage of the reaction above —20 °C. [Pg.65]


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