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Bubbles quality

It is of vital importance that the distance between the lower edge of the feeder and the glass surface is set at a defined value. The striation and the bubble quality are decisively affected by the maintenance of a defined spacing. For this purpose, the casting mould is continuously lowered with a lifting platform. [Pg.136]

The oil and gas samples are taken from the appropriate flowlines of the same separator, whose pressure, temperature and flowrate must be carefully recorded to allow the recombination ratios to be calculated. In addition the pressure and temperature of the stock tank must be recorded to be able to later calculate the shrinkage of oil from the point at which it is sampled and the stock tank. The oil and gas samples are sent separately to the laboratory where they are recombined before PVT analysis is performed. A quality check on the sampling technique is that the bubble point of the recombined sample at the temperature of the separator from which the samples were taken should be equal to the separator pressure. [Pg.113]

BWRs do not operate with dissolved boron like a PWR but use pure, demineralized water with a continuous water quality control system. The reactivity is controlled by the large number of control rods (>100) containing burnable neutron poisons, and by varying the flow rate through the reactor for normal, fine control. Two recirculation loops using variable speed recirculation pumps inject water into the jet pumps inside of the reactor vessel to increase the flow rate by several times over that in the recirculation loops. The steam bubble formation reduces the moderator density and... [Pg.211]

A top-quality London hotel was horrified to find that its house champagne, for which it charged 60 per bottle, lost its bubbles a few moments after it was poured. At first the hotel blamed the suppliers, but... [Pg.386]

Capacity Quite similar to sieve tray, as high or higher than bubble cap tray from 50% up to 100% design rate (varies with system and design criteria). Performance at specification quality falls off at lower rates. [Pg.124]

Quality of a Wet Vapor, in the vapor-liquid region of a pure substance, the composition of a two-phase system (at given T and P) varies from pure saturated liquid at the bubble jjoint M to pure saturated vapor at the dew point N along the line MQN on the P- V diagram (Figure 2-80). For a wet vapor represented by an intermediate... [Pg.345]

The foam volume and stability of alcohol sulfates is relatively increased in hard water compared to soft water. The amount and quality of foam is dependent on the alkyl length. Sulfates with C12-C,4 alkyl chains produce the richest creamy foam with small bubbles. C8-C10 alcohol sulfates are foam depressants and C16-C18 alcohol sulfates are poor foaming surfactants. Foams produced by alcohol sulfates are also relatively stable in the presence of sebum. Sodium and ammonium alcohol sulfates foam better than triethanolamine alcohol sulfates. Alcohol ether sulfates produce lighter foams than those of alcohol... [Pg.265]

Two-phase heat transfer in micro-channel heat sink was associated with different mechanisms for low, medium, and high-quality flows. Bubble flow and nucleate boiling occur only at low qualities (Xe < 0.05) corresponding to very low heat fluxes. High fluxes produce medium-quality (Xe = 0.05—0.55) or high-quality (Xe = 0.55—1.0) flows depending on the flow rate, where heat transfer is dominated by annular film evaporation. Due to the large differences in heat transfer mechan-... [Pg.336]

The micro bubble column comprises internal cooling via heat conduction from the reaction zone to a mini channel heat exchanger [3, 9, 10], Either two such heat exchange plates can encompass the reaction plate, or only one. In the latter case, the free position is occupied by an inspection window which allows direct observation of the quality of the flow patterns. [Pg.583]

The content of the gas is called quality therefore a 70 quality contains 70% gas. Recently, foams with 95% gas have been examined. For such foam types, only foam prepared from 2% of an anionic surfactant with plain water had uniform, fine-bubble structure [782]. [Pg.267]

The study of flotation kinetics relates to a number of mass transfer processes and these are listed in Table 2.8. The term, entrainment which figures in the mass transfer process statements made in Table 2.8 may be elaborated. It is the process by which particles enter the base of a flotation froth and are transferred up and out of the flotation cell suspended in the water between bubbles. Entrainment should be distinguished from true flotation, whereby particles come out of the cell attached to bubble surfaces. True flotation is chemically selective, while the entrainment process recovers both gangue and valuable minerals alike. Entrainment harms the product grade since recovery of the more abundant gangue mineral reduces the quality of the concentrate. This is especially true in the processing of fine ores. Much flotation research has dealt with reducing entrainment in order to improve... [Pg.191]

The basic mechanism of dryout almost invariably involves the rupture of a residual thin liquid film, either as a microlayer underneath the bubbles or as a thin annular layer in a high-quality burnout scenario. Bankoff (1994), in his brief review of significant progress in understanding the behavior of such thin films, discussed some significant questions that still remain to be answered. [Pg.147]

For diabatic flow, that is, one-component flow with subcooled and saturated nucleate boiling, bubbles may exist at the wall of the tube and in the liquid boundary layer. In an investigation of steam-water flow characteristics at high pressures, Kirillov et al. (1978) showed the effects of mass flux and heat flux on the dependence of wave crest amplitude, 8f, on the steam quality, X (Fig. 3.46). The effects of mass and heat fluxes on the relative frictional pressure losses are shown in Figure 3.47. These experimental data agree quite satisfactorily with Tarasova s recommendation (Sec. 3.5.3). [Pg.232]

C) The DNB in a low-quality froth flow is caused by a bubble burst under the bubbly liquid layer. [Pg.342]


See other pages where Bubbles quality is mentioned: [Pg.568]    [Pg.1571]    [Pg.134]    [Pg.728]    [Pg.513]    [Pg.78]    [Pg.206]    [Pg.281]    [Pg.550]    [Pg.209]    [Pg.237]    [Pg.248]    [Pg.22]    [Pg.45]    [Pg.46]    [Pg.48]    [Pg.91]    [Pg.94]    [Pg.281]    [Pg.321]    [Pg.335]    [Pg.337]    [Pg.557]    [Pg.459]    [Pg.87]    [Pg.166]    [Pg.177]    [Pg.184]    [Pg.191]    [Pg.288]    [Pg.293]    [Pg.340]    [Pg.341]    [Pg.353]    [Pg.358]   
See also in sourсe #XX -- [ Pg.150 ]




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