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Wall Resistance

With the usual materials of construction of heat transfer surfaces, the magnitudes of their thermal resistances may be comparable with the other prevailing resistances. For example, heat exchanger tubing of 1/16 in. wall thickness has these values of 1 fh = L/k for several common materials  [Pg.182]

The Nusselt number, hL/k = h/(k/L), is the ratio of effective heat transfer to that which would take place by conduction through a film of thickness L. [Pg.182]

The Peclet number, DGC/k = GC/(k/D) and its modification, the Graetz number wC/kL, are ratios of sensible heat change of the flowing fluid to the rate of heat conduction through a film of thickness D or L. [Pg.182]

The Prandtl number, Cu/k = (p/p)/(k/pC), compares the rate of momentum transfer through friction to the thermal diffusivity or the transport of heat by conduction. [Pg.182]

The Grashof number is interpreted as the ratio of the product of the buoyancy and inertial forces to the square of the viscous forces. [Pg.182]

Carbon steel Stainless steel Aluminum Glass [Pg.182]


In general, many species of algae have cell walls resistant to digestive enzymes, dark colors, and bitter flavor. AH of these characteristics must be altered to make an acceptable food or feed product. [Pg.465]

Overall coefficients are determined hke shell and tube exchangers that is, sum all the resistances, then invert. The resistances include the hot-side coefficient, the cold-side coefficient, the fouhng factor (usually only a total value not individual values per fluid side) and the wall resistance. [Pg.1085]

For overall tubeside plus shellside fouling use experience factors or 0.002 for most services and 0.004 for extremely fouling materials. Neglect metal wall resistance for overall heat transfer coefficient less than 200 or heat flux less than 20,000. These will suffice for ballpark work. [Pg.31]

Reduce wall resistivity, possibly to less than 10 2-m. [Pg.113]

Note the relative effects of the tube wall resistance when compared to the fouling factors in this case. [Pg.90]

Tables 10-16, 10-17, 10-18, and 10-18A give general estimating overall coefficients, and Table 10-19 gives the range of a few common film coefficients. Table 10-20 illustrates the effect of tube-wall resistance for some special construction materials. Table 10-20A lists estimating coefficients for glass-lined vessels. Also see Reference 215. See Table 10-24 for suggested water rates inside tubes. Tables 10-16, 10-17, 10-18, and 10-18A give general estimating overall coefficients, and Table 10-19 gives the range of a few common film coefficients. Table 10-20 illustrates the effect of tube-wall resistance for some special construction materials. Table 10-20A lists estimating coefficients for glass-lined vessels. Also see Reference 215. See Table 10-24 for suggested water rates inside tubes.
Figure 10-45 can be used to solve the overall coefficient, U, equation for the clean coefficient, composed of the tube-side and shell-side film coefficients only. Correction for tube-side and shell-side scaling and tube-wall resistance can... [Pg.93]

Calculate the overall coefficient using Equation 10-37. Neglect the tube-wall resistance, unless special situations indicate that it should be included. [Pg.111]

Usually the tube wall resistance can be neglected, but if you doubt its effect, add to the resistances. [Pg.124]

For overall U cooling, assume water side fouling = 0.002 propylene side fouling = 0.001 neglect tube wall resistance... [Pg.137]

The tube density coefficient, c[), is given in Table 10-27. The tube wall resistance cannot be ignored for reboilers. Based on the outside tube diameter, ... [Pg.170]

Calculate the required area, based on the film coefficient of steps 4 and 5 together with fouling and tube wall resistances A = Q/U At. [Pg.174]

Plot this point as on Figure 10-123. Because the correlation is based on 14 BWG Admiralty tubes, no correction -was made for tube -wall resistance. [Pg.206]

Wall Resistance Factors— Cast Iron Cooling Sections ... [Pg.209]

Assume a temperature drop across the boiling film, Atj,. Neglect tube wall resistance. [Pg.226]

This section is concerned with the UA xtiT — Text) term in the energy balance for a stirred tank. The usual and simplest case is heat transfer from a jacket. Then A xt refers to the inside surface area of the tank that is jacketed on the outside and in contact with the fluid on the inside. The temperature difference, T - Text, is between the bulk fluid in the tank and the heat transfer medium in the jacket. The overall heat transfer coefficient includes the usual contributions from wall resistance and jacket-side coefficient, but the inside coefficient is normally limiting. A correlation applicable to turbine, paddle, and propeller agitators is... [Pg.176]

For the purpose of comparison, now neglect the wall resistance and difference between the inside and outside tube diameters. From Equation 15.79 ... [Pg.337]

Table 5.17 gives estimates of the film transfer coefficients of an existing shell-and-tube heat exchanger, assuming the tube-wall resistance to be negligible. [Pg.355]

Different factors contribute to the mechanical properties of plant tissue cell turgor, which is one of the most important ones, cell bonding force through middle lamella, cell wall resistance to compression or tensile forces, density of cell packaging, which defines the free spaces with gas or liquid, and some factors, also common to other products, such as sample size and shape, temperature, and strain rate (Vincent, 1994). Depending on the sample properties (mainly turgor and resistance of middle lamella), two failure modes have been described (Pitt, 1992) cell debonding and cell rupture. [Pg.205]

The main changes induced by an osmotic treatment affecting the mechanical behavior of plant tissues are loss of cellular turgor, alteration of middle lamella (Alzamora et al., 1997), alteration of cell wall resistance, establishment of water and solute concentration profiles (Salvatori et al.,... [Pg.205]

Situations will occur where a ductile bending mechanism is not attainable. Deep roof diaphragms and side walls resisting in-plane shear are two examples. For these cases, the response must be limited accordingly. Refer to Chapter 5 for these limits. [Pg.56]

This type of construction uses precast concrete walls with steel or concrete frames (Figure 4.2). The frame resists all vertical loads and precast shear walls resist lateral loads. Ductile connections for precast panels are an important consideration. Precast panels are made with embedded steel connection devices attached to the building frame by bolting or welding. The roof is usually a concrete slab on metal deck. The metal deck is attached to steel framing by studs or puddle welds. Tins type of construction can be economically designed to withstand blast loading on the order of 7 to 10 psi (48 to 69 kPa) side-on overpressure. [Pg.160]

Total resistance = Chest wall resistance + lung resistance... [Pg.142]

It appears that qualitative correlations between antibacterial activity and rate constants of HO ion catalyzed hydrolysis are fortuitous since many factors other than transpeptidase acylation contribute to antimicrobial activity. These other contributing factors include permeation of the outer membrane of the bacterial cell wall, resistance to /3-lactamase, the fit in the active site of the enzyme, stability of the acylated enzyme, and, last but not least, in vivo pharmacokinetic behavior. [Pg.212]

The last term on the left-hand side of eq. (3.301) corresponds to the heat transfer to the external fixed-bed wall. The overall heat transfer resistance is the sum of the internal, external, and wall resistances. In an adiabatic operation, the overall heat transfer coefficient is zero so the corresponding term in the energy balance expression drops out, while in an isothermal operation this coefficient is infinite, so that 7 f 7 s 7W. [Pg.146]

In critically ill patients who have ventilatory failure from various causes (eg, severe bronchospasm, pneumonia, chronic obstructive airway disease), it may be necessary to control ventilation to provide adequate gas exchange and to prevent atelectasis. In the ICU, neuromuscular blocking drugs are frequently administered to reduce chest wall resistance (ie, improve thoracic compliance) and ineffective spontaneous ventilation in intubated patients. [Pg.590]

Susceptible strains of Mycobacterium tuberculosis and other mycobacteria are inhibited in vitro by ethambutol, 1-5 mcg/mL. Ethambutol inhibits mycobacterial arabinosyl transferases, which are encoded by the embCAB operon. Arabinosyl transferases are involved in the polymerization reaction of arabinoglycan, an essential component of the mycobacterial cell wall. Resistance to ethambutol is due to mutations resulting in overexpression of emb gene products or within the embB structural gene. [Pg.1046]


See other pages where Wall Resistance is mentioned: [Pg.583]    [Pg.1034]    [Pg.1042]    [Pg.620]    [Pg.621]    [Pg.88]    [Pg.125]    [Pg.136]    [Pg.171]    [Pg.173]    [Pg.209]    [Pg.230]    [Pg.233]    [Pg.233]    [Pg.233]    [Pg.263]    [Pg.385]    [Pg.142]    [Pg.85]    [Pg.433]    [Pg.193]    [Pg.194]    [Pg.182]   


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