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Balanced pressure

A balanced pressure drop maybe assumed in the horizontal condenser where partial condensation is occurring. [Pg.59]

Balanced pressure loss method. This is a method which is used to improve the performance of a preliminary design of a duct system and reduce the number of control dampers. [Pg.787]

This means that thermostatic balanced pressure steam traps which open when their element senses a temperature somewhat below that of saturated steam at the pressure existing within the steam space are very effective when used as automatic air vents. They are connected to a steam space at any location where air will collect. Usually this means at any remote point from the steam entry, along the path the steam takes as it fills the steam space. [Pg.325]

The groupings then may be described as mechanical, which will include both ball float and inverted bucket steam traps thermostatic, which will include both balanced pressure and bimetallic elements and thermodynamic or disc pattern traps (Figure 22.13). Each type of trap has its own characteristics, and these will make one pattern of trap more suitable for use on a given application than another. In practice, it is usual to find that the applications in any given plant fall into a small number of categories, and it often is possible to standardize on a quite small number of trap types. [Pg.328]

Balanced-pressure steam trap Figure 22.13 Steam traps... [Pg.329]

Methods that utilize external pumps or pressure to inject concentrate into the water stream at a fixed ratio (balanced pressure systems). [Pg.211]

The balanced pressure proportioning system is ideal for large systems, concentrate requirements exceeding 1,000 gal (3,800 I), and for most mobile foam apparatus. [Pg.211]

Turn on the microinjector and open the pressure valve. The injection pressure should be set between 10 and 20 psi with the balance pressure set between 0.2 and 0.4 psi (19). This will prevent medium from flowing back into the needle and diluting the injectable or introducing contamination. [Pg.398]

FIG 12 - SINGLE-SHELL, DIRECT ROTARY DRYER USING STEAM-HEATED AIR AND BALANCED PRESSURE BY MEANS OF A BLOWER AND EXHAUSTER... [Pg.458]

Figure 7. Flow and instrumentation diagram for high temperature, balanced pressure bench-scale unit. LR, level recorder LT, level transmitter TR, temperature recorder FR, pressure recorder FR, flow recording RD, densitometer PC, pressure controller TC, temperature controller GM, gas meter F, filter VSD, variable speed drive PCV, pressure regulator CV, control valve SV, solenoid valve S, gamma ray source. Figure 7. Flow and instrumentation diagram for high temperature, balanced pressure bench-scale unit. LR, level recorder LT, level transmitter TR, temperature recorder FR, pressure recorder FR, flow recording RD, densitometer PC, pressure controller TC, temperature controller GM, gas meter F, filter VSD, variable speed drive PCV, pressure regulator CV, control valve SV, solenoid valve S, gamma ray source.
Figure 8. High temperature, balanced pressure reactor... Figure 8. High temperature, balanced pressure reactor...
Figure 4.1 Schematic diagram of a coupled column system. The first column (ID) is connected to the second column (2D) through the interface or valve system. The interface can be a direct coupling, a live T-union, a complex multiport valve, or a thermal or cryogenic modulation system. The stimulus can be the switching of the valve, a balancing pressure to divert flow towards 2D, an added flow that is used in pressure tuning, or the drive mechanism for the modulator. The line to detector 1 will normally be a non-retaining section of column. In a two-oven system, ID and 2D will be in different ovens the dotted line indicates separately heated zones. Figure 4.1 Schematic diagram of a coupled column system. The first column (ID) is connected to the second column (2D) through the interface or valve system. The interface can be a direct coupling, a live T-union, a complex multiport valve, or a thermal or cryogenic modulation system. The stimulus can be the switching of the valve, a balancing pressure to divert flow towards 2D, an added flow that is used in pressure tuning, or the drive mechanism for the modulator. The line to detector 1 will normally be a non-retaining section of column. In a two-oven system, ID and 2D will be in different ovens the dotted line indicates separately heated zones.
As a consequence of surface tension, there is a balancing pressure difference across any curved surface, the pressure being greater on the concave side. For a curved surface with principal radii of curvature rj and r2 this pressure difference is given by the Young-Laplace equation, Ap = y(llrx + l/r2), which reduces to Ap = 2y/r for a spherical surface. [Pg.67]

Figure 4.3. Steps for balanced pressure sampling in GC headspace analysis. [Reprinted with permission from Ref. 11 (Fig. 6, p. 208). Copyright John Wiley Sons.]... Figure 4.3. Steps for balanced pressure sampling in GC headspace analysis. [Reprinted with permission from Ref. 11 (Fig. 6, p. 208). Copyright John Wiley Sons.]...
By ruling out gravitational and acceleration forces, we are left with a simple balance pressure acting against viscous forces. By considering a symmetric cylindrical tube, we have a geometry so simple that this balance can be easily formulated and the flow equations readily solved. [Pg.58]

We note that our previous descriptions of flow processes have tacitly assumed laminar flow. For example, flow in capillaries was described by balancing pressure-derived forces against viscous forces, ignoring acceleration (inertial) effects. Darcy s law, Eq. 4.18, is also based on laminar flow. With turbulence, flow resistance increases the pressure gradient is no longer linearly related to flow (see Eqs. 4.18 through 4.20) but increases more rapidly as expressed by... [Pg.75]

Chromatographic System (See Chromatography, Appendix IIA.) Use a gas chromatograph equipped with a balanced pressure automatic headspace sampler and a flame-ionization detector and that contains a 50-m x 0.32-mm fused silica capillary column bonded with a 5-p.m film of 5% phenyl-95 % methylsiloxane, or equivalent. Program the column temperature from 70° to 250° at 107min, with the transfer line at 140° and the detector at 250°. Use helium as the carrier gas, flowing at a rate of about 0.8 mL/min. On... [Pg.341]

This system of metal blocks and spacer is then layered between two heat-insulating plates of low-thermal-conductivity material and another two plates with high mechanical rigidity (e.g. of light aluminum alloy). The overall system is fixed with a system of torque-controlled screws, the balanced pressure providing channel sealing. [Pg.110]

In order to be uniformly filled in a commercial reactor without causing flow distribution problems, an industrial catalyst must be formed in a certain shape and size. The specifications for catalyst size, shape, and mechanical strength are decided in accordance with the energy balance, pressure drop, and flow dynamics of the reactor design. [Pg.356]

As a consequence of surface tension, there Is a balancing pressure difference across any curved Interface. Thus, the vapor pressure over a concave liquid surface will be smaller than that over a corresponding flat surface. This vapor pressure difference can be calculated from the Kelvin s equation ... [Pg.276]


See other pages where Balanced pressure is mentioned: [Pg.786]    [Pg.1002]    [Pg.76]    [Pg.77]    [Pg.278]    [Pg.100]    [Pg.594]    [Pg.982]    [Pg.81]    [Pg.77]    [Pg.186]    [Pg.7]    [Pg.311]    [Pg.334]    [Pg.93]    [Pg.434]    [Pg.611]    [Pg.1326]    [Pg.328]    [Pg.1045]    [Pg.425]    [Pg.193]    [Pg.1388]    [Pg.239]    [Pg.318]    [Pg.348]   
See also in sourсe #XX -- [ Pg.323 ]




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