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HACKING

In Fig. 8.3, the only cost forcing the optimal conversion hack from high values is that of the reactor. Hence, for such simple reaction systems, a high optimal conversion would he expected. This was the reason in Chap. 2 that an initial value of reactor conversion of 0.95 was chosen for simple reaction systems. [Pg.243]

While you may not necessarily perceive the difference, HyperChem is designed to consist of two basic components d Ironi end an d a hack end. [Pg.155]

VR, the inputs correspond to the value of the various parameters and the network is 1 to reproduce the experimentally determined activities. Once trained, the activity of mown compound can be predicted by presenting the network with the relevant eter values. Some encouraging results have been reported using neural networks, have also been applied to a wide range of problems such as predicting the secondary ire of proteins and interpreting NMR spectra. One of their main advantages is an to incorporate non-linearity into the model. However, they do present some problems Hack et al. 1994] for example, if there are too few data values then the network may memorise the data and have no predictive capability. Moreover, it is difficult to the importance of the individual terms, and the networks can require a considerable 1 train. [Pg.720]

This type of titration is called a hack titration. [Pg.275]

To the above costs must he added hack any unit costs omitted from those to which learning might bring improvement. These will normally include overheads and specific charges on the project such as the unit cost of special tools, jigs, etc. [Pg.821]

This specification covers horizontal, end suction, vertically split, single-stage centrifugal pumps with top centerline discharge and hack pullout feature. [Pg.918]

G External weld reinforcement and internal weld protrusion shall he fused with and shall merge smoothly into the component surface. The thickness of external weld reinforcement and internal weld protrusion (when no hacking ring is used) shall not exceed the following ... [Pg.1007]

FIG. 11-36 Heat-exchanger-component nomenclature, (a) Internal-floating-head exchanger (with floating-head hacking device). Type AES. (h) Fixed-tiihe-sheet exchanger. Type BEM. (Standard of Tiihiilar Exchanger Manufacturers Association, 6th ed., 1978. )... [Pg.1066]

FIG. 23-3 Temperature and composition profiles, a) Oxidation of SOp with intercooling and two cold shots, (h) Phosgene from GO and Gfi, activated carbon in 2-in tubes, water cooled, (c) Gumene from benzene and propylene, phosphoric acid on < uartz, with four quench zones, 260°G. (d) Mild thermal cracking of a heavy oil in a tubular furnace, hack pressure of 250 psig and sever heat fluxes, Btu/(fr-h), T in °F. (e) Vertical ammonia svi,ithesizer at 300 atm, with five cold shots and an internal exchanger. (/) Vertical methanol svi,ithesizer at 300 atm, Gr O -ZnO catalyst, with six cold shots totaling 10 to 20 percent of the fresh feed. To convert psi to kPa, multiply by 6.895 atm to kPa, multiply by 101.3. [Pg.2072]

The internal volute wall and/or hack plate on pumps with open and semi open impellers. [Pg.136]

Hack, K. (editor) (1996) The SGTE Casebook Thermodynamics at Work (The Institute of Materials, London). [Pg.486]

Receive instructions to pump on job card, paper, or phone. Confirm hack instructions and then enter specifications on log book and record card. [Pg.324]

Figures 13.8 and 13.9 show the separation of polystyrene standards using a typical mixed-bed column and its calibration plot, respectively. The major advantages of using a large i.d. 10-mm column are low hack pressure and relatively short run times. As seen in Fig. 13.8,10 standards from toluene thru 8.4 X 10 MW can be resolved in a mere 21 min. Because of the large 10-mm i.d. columns, 1.5-ml/min flow rates give a linear velocity equivalent to that of only 0.9 ml/min using a 7.6-mm i.d. column. Also, the gel volume contained in one 10 mm i.d. X 500 mm column is 39.3 ml, whereas a 7.6 mm i.d. X 300 mm column contains only 13.6 ml of gel volume. This bulk volume factor, combined with the large pore volumes of gels, obtains essentially the same resolution as that obtained on three standard 7.6 X 300-mm columns in series, but in about one-half the usual time required using the smaller columns. Figures 13.8 and 13.9 show the separation of polystyrene standards using a typical mixed-bed column and its calibration plot, respectively. The major advantages of using a large i.d. 10-mm column are low hack pressure and relatively short run times. As seen in Fig. 13.8,10 standards from toluene thru 8.4 X 10 MW can be resolved in a mere 21 min. Because of the large 10-mm i.d. columns, 1.5-ml/min flow rates give a linear velocity equivalent to that of only 0.9 ml/min using a 7.6-mm i.d. column. Also, the gel volume contained in one 10 mm i.d. X 500 mm column is 39.3 ml, whereas a 7.6 mm i.d. X 300 mm column contains only 13.6 ml of gel volume. This bulk volume factor, combined with the large pore volumes of gels, obtains essentially the same resolution as that obtained on three standard 7.6 X 300-mm columns in series, but in about one-half the usual time required using the smaller columns.

See other pages where HACKING is mentioned: [Pg.319]    [Pg.325]    [Pg.325]    [Pg.325]    [Pg.325]    [Pg.744]    [Pg.156]    [Pg.157]    [Pg.63]    [Pg.63]    [Pg.304]    [Pg.363]    [Pg.387]    [Pg.38]    [Pg.10]    [Pg.466]    [Pg.283]    [Pg.219]    [Pg.219]    [Pg.918]    [Pg.918]    [Pg.739]    [Pg.402]    [Pg.79]    [Pg.150]    [Pg.485]    [Pg.548]    [Pg.598]    [Pg.287]    [Pg.893]    [Pg.981]    [Pg.363]    [Pg.8]    [Pg.123]    [Pg.128]    [Pg.159]   
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See also in sourсe #XX -- [ Pg.265 ]

See also in sourсe #XX -- [ Pg.6 ]




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