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The Hydraulic Equations

Column pressure drop is a function of tray (or packing) type and design and column operating conditions, information that is required for the estimation of the mass transfer coefficients. It is, therefore, possible to add a pressure drop equation to the set of independent equations for each stage and to make the pressure of each stage (tray or packed section) an unknown variable. The stage is assumed to be at mechanical equilibrium SOP/ = P/=P.. [Pg.402]

The pressure of the top tray (or top of the packing) must be specified along with the pressure of any condenser. The pressure of trays (or packed sections) below the topmost are calculated from the pressure of the stage above and the pressure drop on that tray (or over that packed section). [Pg.402]

If the column has a condenser, which is numbered as stage 1 here, the hydraulic [Pg.403]

If the top stage is not a condenser, the hydraulic equations are expressed as follows  [Pg.403]

The pressure drop over sieve and valve trays may be estimated using correlations presented by Lockett (1986) and Kister (1992). For bubble cap trays the procedures described by Bolles (1963) can be adapted for computer based calculation. Kister (1992) reviews the methods available for estimating the pressure drop in dumped packed columns. The pressure drop in structured packed columns may be estimated using the method of Bravo et al. (1986). [Pg.403]


According to the hydraulic equation, arterial blood pressure (BP) is directly proportionate to the product of the blood flow (cardiac output, CO) and the resistance to passage of blood through precapillary arterioles (peripheral vascular resistance, PVR) ... [Pg.222]

Now the left-hand side of Equation (3.54) is equal to the hydraulic radius r of the group of cores (cf. Equation (3.49)) and the right-hand side by the Kelvin equation (cf. Equation (3.20)) is equal to rjl. Consequently,... [Pg.149]

The most important transition velocity, often regarded as the minimum transport or conveying velocity for settling slurries, is V 9- The Durand equation (Durand, Minnesota Int. Hydraulics Conf., Proc., 89, Int. Assoc, for Hydraulic Research [1953] Durand and Condohos, Proc. Colloq. On the Hyd. Tran.spoti of Solids in Pipes, Not. Cool Boord [UK], Paper IV, 39-35 [1952]) gives the minimum transport velocity as... [Pg.657]

Table 5-2 shows the equations for calculating the hydraulic diameter for various flame arrester passageways. [Pg.107]

To monitor the motors performance, a plot can be made in real time of the mechanical horsepower versus the hydraulic horsepower. The curve should be similar to the MHP curve of Figure 4-315 since, according to equation 4-233, at constant Q, the hydraulic power is proportional to AP, An example is shown in Figure 4-317 where measurements have been made at various RPM. [Pg.1029]

This expression gives D2 as a function of the conditions at the upstream side of the hydraulic jump. The corresponding velocity u2 is obtained by substituting in the equation ... [Pg.102]

For the heat transfer for fluids flowing in non-circular ducts, such as rectangular ventilating ducts, the equations developed for turbulent flow inside a circular pipe may be used if an equivalent diameter, such as the hydraulic mean diameter de discussed previously, is used in place of d. [Pg.433]

CARPENTER et alS35) suggest using the hydraulic mean diameter de = dj — d i) in the Sieder and Tate equation (9.66) and recommend the equation ... [Pg.433]

Equation (26) gives values of Lp equal to 10-16 pipe diameters for Re between 2500 and 20 000. According to Davies [91] these are the lowest estimate of the hydraulic entry length. In practice the observed values are often in the range of 25 to 100 pipe diameters. [Pg.101]

The heat transfer coefficient to the vessel wall can be estimated using the correlations for forced convection in conduits, such as equation 12.11. The fluid velocity and the path length can be calculated from the geometry of the jacket arrangement. The hydraulic mean diameter (equivalent diameter, de) of the channel or half-pipe should be used as the characteristic dimension in the Reynolds and Nusselt numbers see Section 12.8.1. [Pg.777]

The airflow equations presented above are based on the assumption that the soil is a spatially homogeneous porous medium with constant intrinsic permeability. However, in most sites, the vadose zone is heterogeneous. For this reason, design calculations are rarely based on previous hydraulic conductivity measurements. One of the objectives of preliminary field testing is to collect data for the reliable estimation of permeability in the contaminated zone. The field tests include measurements of air flow rates at the extraction well, which are combined with the vacuum monitoring data at several distances to obtain a more accurate estimation of air permeability at the particular site. [Pg.530]

The most important factor for movement in the saturated zone is the hydraulic gradient. The velocity head, which is generally more than ten orders of magnitude smaller than the pressure and gravitational head, may be neglected because of the slow water movement. Equation 18.4 can therefore be simplified to... [Pg.701]

Theoretical estimation of water flow in unsaturated soils is difficult and complex. The derivation of the versions of the Richards equation commonly solved in modern models required several assumptions. In addition, it is difficult to accurately estimate likely field values for unsaturated soil hydraulic conductivity on the scale of a complete ET cover. Nevertheless, the Richards equation provides useful estimates of flow of water within the soil where adequate estimates of soil hydraulic conductivity are available. [Pg.1069]

Figure 26.9 illustrates Darcy s law, the basic equation used to describe the flow of fluids through porous materials. In Darcy s law, the coefficient k, hydraulic conductivity, is often called the coefficient of permeability by civil engineers. [Pg.1106]

The tests do not directly measure the hydraulic conductivity k of the soil. Instead they measure the infiltration rate / for the soil. Since hydraulic conductivity is the infiltration rate divided by the hydraulic gradient i (see equations in Figure 26.14), it is necessary to determine the hydraulic gradient before k can be calculated. The following equation (with terms defined in Figure 26.14) can be used to estimate the hydraulic gradient ... [Pg.1114]

Transmissivity is simply the coefficient of permeability, or the hydraulic conductivity (k), within the plane of the material multiplied by the thickness (T) of the material. Because the compressibility of some polymeric materials is very high, the thickness of the material needs to be taken into account. Darcy s law, expressed by the equation Q = kiA, is used to calculate the rate of flow, with transmissivity equal to kT and i equal to the hydraulic gradient (see Figure 26.22) ... [Pg.1130]

Cheremisinoff and Davis (1979) relaxed these two assumptions by using a correlation developed by Cohen and Hanratty (1968) for the interfacial shear stress, using von Karman s and Deissler s eddy viscosity expressions for solving the liquid-phase momentum equations while still using the hydraulic diameter concept for the gas phase. They assumed, however, that the velocity profile is a function only of the radius, r, or the normal distance from the wall, y, and that the shear stress is constant, t = tw. ... [Pg.213]

The evaluation of the parameters for this flow regime requires the calculation of the Reynolds number and hydraulic diameter for each continuous phase. The hydraulic diameter can be determined only if the holdup of each phase is known. This again illustrates the importance of understanding the fluid mechanics of two phase systems. Once the hydraulic diameter is known, the Reynolds number can be evaluated with the knowledge of the in situ phase velocity, and the parameters of the model equations can be evaluated. [Pg.31]

All the relationships presented in Chapter 6 apply directly to circular pipe. However, many of these results can also, with appropriate modification, be applied to conduits with noncircular cross sections. It should be recalled that the derivation of the momentum equation for uniform flow in a tube [e.g., Eq. (5-44)] involved no assumption about the shape of the tube cross section. The result is that the friction loss is a function of a geometric parameter called the hydraulic diameter ... [Pg.195]

The hydraulic characteristics of the flow were calculated according to the Manning equation. [Pg.118]

The hydraulic performance of sewer pipes can be described at different levels. In the case of nonstationary, nonuniform flow, the Saint Venant Equations should be applied. However, under dry-weather conditions, the Manning Equation is an adequate description of the wastewater flow in a gravity sewer pipe when considering the prediction of wastewater quality changes under transport. There are no grounds for using advanced hydraulic models because of the uncertainties in the prediction of the microbial transformations of the wastewater. [Pg.213]

The Manning Equation and the Equation of Continuity are the basic hydraulic tools for description of the wastewater flow in a pipe at stationary, uniform flow ... [Pg.213]

Relation 9.77 is usually called the Washburn equation [55,237], One should consider it as a special case of the fundamental Young-Laplace equation [3,9-11], Washburn was the first to propose the use of mercury for measurements of porosity. Now, it is a common method [3,8,53-55] of psd measurements for a range of sizes from several hundreds of microns to 3 to 6 nm. The lower limit is determined by the maximum pressure, which is applied in a mercury porosimeter the limiting size of rWl = 3 nm is achieved under PHg = 4000 bar. The measurements are carried out after vacuum treatment of a sample and filling the gaps between pieces of solid with mercury. Further, the hydraulic system of a device performs the gradual increase of PHg, and the appropriate intmsion of mercury in pores of the decreasing size occurs. [Pg.321]

The tensile test is performed by placing a specially shaped specimen in the heads of the testing machine. The specimen is pulled apart through a hydraulic or mechanical loading system (Figure 15.33). Most ordinary tensile tests are conducted at room temperature and the tensile load is applied slowly. The unit measure of tensile strength is the pascal (Pa), or newtons per square meter (N-nf2), and is defined by the following equation ... [Pg.450]


See other pages where The Hydraulic Equations is mentioned: [Pg.532]    [Pg.402]    [Pg.532]    [Pg.532]    [Pg.402]    [Pg.532]    [Pg.668]    [Pg.161]    [Pg.365]    [Pg.96]    [Pg.430]    [Pg.115]    [Pg.119]    [Pg.96]    [Pg.186]    [Pg.249]    [Pg.780]    [Pg.1174]    [Pg.1174]    [Pg.524]    [Pg.74]    [Pg.144]    [Pg.548]    [Pg.350]    [Pg.93]    [Pg.55]    [Pg.78]   


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