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Operator charge

The question of whether it is necessary to break down a particular operation to a finer level of detail depends on whether the analyst believes that a significant error mode is likely to be revealed by a more fine grained analysis. For example, the operation "charge the reactor" may be an adequate level of description if the analyst believes that the likelihood of error is low, and/or the consequences of error are not severe. However, if this operation was critical, it could be further redescribed as shown below ... [Pg.163]

If the consequences of not waiting until the pressure had dropped were serious and/or omitting to check the pressure was likely, then it would be necessary to break down the operation "charge reactor" to its component steps. This approach to deciding on the level of decomposition is called the PxC rule (where P is the probability of failing to carry out an operation and C the cost of the consequences). The size of the product PxC determines whether or not to describe the operation in more detail (Shepherd, 1985). [Pg.163]

An electrochemical cell is a device by means of which the enthalpy (or heat content) of a spontaneous chemical reaction is converted into electrical energy conversely, an electrolytic cell is a device in which electrical energy is used to bring about a chemical change with a consequent increase in the enthalpy of the system. Both types of cells are characterised by the fact that during their operation charge transfer takes place at one electrode in a direction that leads to the oxidation of either the electrode or of a species in solution, whilst the converse process of reduction occurs at the other electrode. [Pg.77]

Plant Location Operator Charge Stock Rated Capacity, Short Tons/Year... [Pg.320]

The operating conditions for the three processes are very similar— only temperatures are somewhat dissimilar. The Shell Development system, employing a modified Friedel-Crafts system, operates at a lower temperature—150°-210°F vs. 250°-400°F for the other two processes. However, the equilibrium effects of the temperature differences are minimized as shown by the similarity in n-C4 and n-C5 yields shown in Table VI. Unleaded octane numbers for C5/C6 isomerate, obtained from a pure C5/C6 straight-run fraction, could not be found in the literature for the Shell process. However, pilot unit operations charging laboratory blends of n-C5, n-C6, and C6 naphthenes have been reported (26, 45). In the Shell process the use of antimony trichloride and hydrogen has considerably reduced the amount of side reactions for a Friedel-Crafts system so that the yield for this process is quite close to the yield structure for the other two processes. [Pg.152]

In operation, charges are first accumulated in the column wells. At the end of the integration period, the voltage levels at the column wells are measured. [Pg.56]

The power-conditioning system (built by GE) is based on GTO thyristor technology and features rapid (4.2 ms) response and bi-directional four-quadrant operation (charge, discharge, and VAR capable), 12-pulse waveform (low distortion), and is self-commutating. It is rated at 1.6-MVA peak (10 s) and at 1-MW continuous power [23]. [Pg.315]

Includes evaporator for concentration of liquid to be permanently stored as well as storage tanks. Storage tanks can be carried as operating charge but interest on investment tied up must be carried. [Pg.466]

The housekeeping involved in batch operation, charging the still and removing quantities of hot residues reduce the available running hours and require operator s time and attention. [Pg.85]

Liang, Y. Baker, M.E. Todd Yeager, B. Bonner Denton, M. Quantitative analysis of aflatoxins by high-performance thin-layer chromatography utilizing a scientifically operated charge-coupled device detector. Anal. Chem. 1996, 68, 3885. [Pg.1547]

The p-gal production flowsheet can be divided into three sections. (1) Fermentation, where E. coli cells are used to produce the P-gal through a fermentation process. The fermentation process consists of four operations charge, reaction, discharge, and clean. [Pg.265]

The fol lowing assumptions were made for each category. Aii outcomes were converted to an houriy operating charge for 8000 hours yeariy operation, with a cieaning cycie time of 20 minutes and an emission time of 2 minutes during that... [Pg.224]


See other pages where Operator charge is mentioned: [Pg.179]    [Pg.817]    [Pg.44]    [Pg.167]    [Pg.576]    [Pg.159]    [Pg.29]    [Pg.202]    [Pg.116]    [Pg.127]    [Pg.268]    [Pg.416]    [Pg.739]    [Pg.128]    [Pg.416]    [Pg.739]    [Pg.399]    [Pg.248]    [Pg.119]    [Pg.191]    [Pg.93]    [Pg.60]    [Pg.165]    [Pg.286]    [Pg.460]    [Pg.159]    [Pg.491]    [Pg.101]    [Pg.188]    [Pg.155]    [Pg.2612]    [Pg.377]    [Pg.413]    [Pg.302]    [Pg.32]    [Pg.85]   
See also in sourсe #XX -- [ Pg.126 ]




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