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Vacuum diagrams

Obviously, we gain precisely the same expressions as in the multi-root theory since we postulated the same form of the effective Hamiltonian. We recall that all matrix elements of the effective Hamiltonian are expressed by means of connected diagrams only in the case of diagonal elements just connected vacuum diagrams may come into consideration and in the case of off-diagonal elements at least one part of a disconnected diagram would correspond to an internal excitation. [Pg.85]

Fig. 2.21 Vacuum diagram - Roots pump with integrated bypass line and backing pump... Fig. 2.21 Vacuum diagram - Roots pump with integrated bypass line and backing pump...
Fig. 2.78 Vacuum diagram for drying of sail Pump combination consisting of Roots pump, condenser and rotary piunger pump for stepwise sviithing of the pumping process (see text)... Fig. 2.78 Vacuum diagram for drying of sail Pump combination consisting of Roots pump, condenser and rotary piunger pump for stepwise sviithing of the pumping process (see text)...
The matrix H i hermitian. By dropping the vacuum diagrams from H, we may also obtain the energy differences AE = E - Eo directly. [Pg.353]

A vacuum diagram is a diagram having only internal fermion lines (i.e. oriented hnes connecting two vertices). [Pg.121]

Linked Cluster Theorem. Only linked (or connected) vacuum diagrams contribute to the energy, while all unlinked (or disconnected) vacuum diagrams mumally cancel out, so that... [Pg.122]

It is apparent that such an approach is not extensive, because the left-hand side is diagrammatically represented by unUnked diagrams which have no counterpart on the right-hand side (a product of a closed vacuum diagram and the cluster amplitude). Nevertheless it may serve as an initial guess when convergence difficulties with the extensive formulations may be expected. This approximation is very similar to... [Pg.154]

A schematic diagram of the apparatus is shown in Figure 3.2. The molecules are introduced under a partial vacuum of 10 torr into a buffer chamber that communicates via molecular slipstream with the source itself at 10 to 10 torr in order to ensure a constant concentration in the source at all times during the analysis. [Pg.47]

Fig. 9. Schematic diagram of the operation of a vacuum leaf filter. Fig. 9. Schematic diagram of the operation of a vacuum leaf filter.
Fig. 11. Schematic diagram of a horizontal belt vacuum filter. Fig. 11. Schematic diagram of a horizontal belt vacuum filter.
The large excess of water from the hydrolysis is removed in a series of multiple-effect evaporators (8), and the ethylene glycol is refined by vacuum distillation. Figure 3 depicts a typical process flow diagram. [Pg.358]

Processes involving oxygen and nitrogen oxides as catalysts have been operated commercially using either vapor- or Hquid-phase reactors. The vapor-phase reactors require particularly close control because of the wide explosive limit of dimethyl sulfide in oxygen (1—83.5 vol %) plants in operation use Hquid-phase reactions. Figure 2 is a schematic diagram for the Hquid-phase process. The product stream from the reactor is neutralized with aqueous caustic and is vacuum-evaporated, and the DMSO is dried in a distillation column to obtain the product. [Pg.111]

The vanadium alloy is purified and consoHdated by one of two procedures, as shown in the flow diagram of the entire aluminothermic reduction process presented in Figure 1. In one procedure, the brittle alloy is cmshed and heated in a vacuum at 1790°C to sublime most of the aluminum, oxygen, and other impurities. The aluminum faciHtates removal of the oxygen, which is the feature that makes this process superior to the calcium process. Further purification and consoHdation of the metal is accompHshed by electron-beam melting of pressed compacts of the vanadium sponge. [Pg.383]

Fig. 11. Flow diagram of the vacuum-freeze (direct) vapor-compression desalination process. Fig. 11. Flow diagram of the vacuum-freeze (direct) vapor-compression desalination process.
The two comparatively new type of breakers, vacuum and SFg are exceptions and have gained favour in view of their reliability and durability. For details on these breakers, see Sections 19.5.5 and 19.5.6, which also deal with their switching behaviour and phenomenon of arc reignition. Figures 12.44 and 12.45 illustrate typical power and control circuit diagrams respectively, for a 6.6 kV breaker-operated motor starter. [Pg.308]

Figure 8.16. Schematic diagram of modulus versus temperature for two materials A and B to be shaped in the rubbery phase in the temperature range T]-T2. In this range the modulus of A is above a critical figure C above which atmospheric pressure is insufficient to shape sheet of a given thickness. Such material could therefore not be vacuum formed. The type B material would, however, present no problem on this score... Figure 8.16. Schematic diagram of modulus versus temperature for two materials A and B to be shaped in the rubbery phase in the temperature range T]-T2. In this range the modulus of A is above a critical figure C above which atmospheric pressure is insufficient to shape sheet of a given thickness. Such material could therefore not be vacuum formed. The type B material would, however, present no problem on this score...
In X-ray photoelectron spectroscopy (XPS), a beam of soft X-rays with energy hv s. focused onto the surface of a solid that is held under an ultra-high vacuum, resulting in the ejection of photoelectrons from core levels of the atoms in the solid [20]. Fig. 15 shows an energy level diagram for an atom and illustrates the processes involved in X-ray-induced photoelectron emission from a solid. [Pg.261]

Figure 2-47. Acceptable pressure losses between the vacuum vessel and the vacuum pump. Note reference sections on figure to system diagram to illustrate the sectional type hook-ups for connecting lines. Use 60% of the pressure loss read as acceptable loss for the system from process to vacuum pump, for initial estimate. P = pressure drop (torr) of line in question Po = operating pressure of vacuum process equipment, absolute, torr. By permission, Ryans, J. L. and Roper, D. L., Process Vacuum System Design Operation, McGraw-Hill Book Co., Inc., 1986 [18]. Figure 2-47. Acceptable pressure losses between the vacuum vessel and the vacuum pump. Note reference sections on figure to system diagram to illustrate the sectional type hook-ups for connecting lines. Use 60% of the pressure loss read as acceptable loss for the system from process to vacuum pump, for initial estimate. P = pressure drop (torr) of line in question Po = operating pressure of vacuum process equipment, absolute, torr. By permission, Ryans, J. L. and Roper, D. L., Process Vacuum System Design Operation, McGraw-Hill Book Co., Inc., 1986 [18].
Figure 6-33 diagrams vacuum system arrangements for process systems. It is important to examine the plant economics for each system plus the performance reliability for maintaining the desired vacuum for process control. [Pg.382]

Figure 6-35. Diagram of liquid ring vacuum pump features. By permission, Nash Engineering Co. Figure 6-35. Diagram of liquid ring vacuum pump features. By permission, Nash Engineering Co.
Figure 1-4. Flow diagram of the Dehydrate process (1) absorption column, (2) glycol sill, (3) vacuum drum. Figure 1-4. Flow diagram of the Dehydrate process (1) absorption column, (2) glycol sill, (3) vacuum drum.

See other pages where Vacuum diagrams is mentioned: [Pg.656]    [Pg.33]    [Pg.33]    [Pg.59]    [Pg.308]    [Pg.24]    [Pg.603]    [Pg.121]    [Pg.235]    [Pg.135]    [Pg.656]    [Pg.33]    [Pg.33]    [Pg.59]    [Pg.308]    [Pg.24]    [Pg.603]    [Pg.121]    [Pg.235]    [Pg.135]    [Pg.204]    [Pg.270]    [Pg.396]    [Pg.445]    [Pg.219]    [Pg.152]    [Pg.246]    [Pg.558]    [Pg.309]    [Pg.262]    [Pg.144]    [Pg.230]    [Pg.181]    [Pg.382]    [Pg.50]   


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