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Cold zones

FW supply and on-off/modulation mechanisms. The on-off supply of FW tends to create cold-zone stratification within the boiler, leading to reduced steam production rates and misting (fogging) in the steam space. Boiler plant designs that provide for the continuous provision of FW through a modulated FW supply prevent these problems. [Pg.280]

The crystal compositions vary, depending on the transport agent used, from TiB,4,y (Ij) and TiBj <,4 (TeCl4). At process temperatures > 1000°C and with I2, the transport direction is reversed. Crystals grow in the cold zone of the tube, but only microscopic needle-like crystals are obtained. ... [Pg.280]

Figure 11.1 shows the pyrogram of lead white pigmented linseed oil paint obtained at 610 °C with a Curie-point pyrolyser, with on-line methylation using 2.5% methanolic TMAH. The pyrolyser was a Curie-point pyrolysis system FOM 5-LX, specifically developed at FOM Amolf Institute (Amsterdam, the Netherlands), to reduce cold spots to a minimum. This means that the sample can be flushed before pyrolysis in a cold zone, and it also ensures optimum pressure condition within the pyrolysis chamber, thus guaranteeing an efficient transport to the GC injection system [12]. [Pg.308]

Secure and isolate the entire incident area and deny entry to all but accredited responders. Assign control areas Hot/Warm/Cold zones. [Pg.63]

Enforce rules for entry into the total area involved, including Hot/Warm/Cold zones. [Pg.63]

Hold a briefing for entry personnel and support crew. Ensure that all staff on scene understand emergency signals, preplanned escape routes, locations of Hot/Warm/ Cold zones, operational hazards at this site, the evacuation system, the buddy system, the need for appropriate personal protective equipment (PPE) the potential need to decontaminate rescuers and their equipment, and contaminated persons location of rehabilitation area, possible air space closure over incident site, etc. [Pg.63]

Decontamination Corridor A corridor that acts as a protective buffer and bridges between the hot zone and the cold zone and is located in the warm zone within which decontamination stations and personnel are located to apply decontamination procedures. [Pg.304]

The synthesis of compounds such as MPS3 (M = Mn, Cd) was performed (Villanueva et al. 2004) in a device consisting of a silica ampoule divided into a Dewar zone (hot zone) and a non-insulated part (cold zone) which can be operated inside domestic microwave ovens. This has been described as a rapid method which involves a heat concentration within the Dewar zone that allows the required temperature for the reaction to be reached. In the specific case a mixture of S, P, and the metal gives MPS3 compounds. The temperature gradient assures the vapour phase transport to the cold zone MPS3 crystals are deposited within a few minutes in this zone. [Pg.574]

It may be shown that the ratio of the concentration in a hot zone to that in a cold zone for recuperative parametric pumping is given by ... [Pg.1044]

Where applicable, thermocouple placement shall be in the container cold zone, as determined from generated container mapping studies. [Pg.280]

If previous empty tunnel heat distribution test runs have identified hot or cold zones, at least one of the penetration test containers must be placed in each of these zones per run. [Pg.280]

At least one set of microbial challenge or penetration test containers shall be placed in the sterilizer cold zone per run (where applicable). [Pg.282]

Cold zone temperature correction must be used where applicable. [Pg.283]

Thermal uniformity in the cold zone was found to be from 0.01 to 0.02 °C, and that in the hot zone was found to be better than + 0.5 °C vertically and + 0.1 °C horizontally. Thermal gradients near the solid-liquid interface were achieved in excess of 30 °C cm " in the crystal region and up to 20 °C cm" in the melt. The growth of crystals was performed in a sealed transparent silica ampoule, which has two rooms for As source and GaAs polycrystalline, respectively, separated by a quartz diffusion barrier. For details of the growth process the reader is referred to Ref. 43. In this experiment the As source temperature T. was systematically reduced by 2 °C at 3 h intervals from 620 °C to 614 °C. [Pg.243]

Analysis of Heat Transfer. In the vertical Bridgman-Stockbarger system shown in Figure la, the axial temperature gradient needed to induce solidification is created by separating hot and cold zones with a diabatic zone in which radial heat flow from the ampoule to the furnace is suppressed. Analyses of conductive heat transfer have focused on this geometry. [Pg.87]

The compound below was prepared by heating a mixture of unligated dirhodium(II) tetra-kis(trifluoroacetate) (0.066 g, 0.10 mmol) and diphenylacetylene (0.036 g, 0.20 mmol) at 65-85°C for 3 days in a sealed evacuated Pyrex ampoule. Dark green block crystals were grown in both hot and cold zones of the tube. Yield 0.058 g (57.2%). [Pg.188]

In GC the injection may take place at a temperature that is lower than that of the column oven. The solute bands will be concentrated in a small volume and may be brought into the column by a subsequent heating of the cold zone. If this zone is part of the column itself we talk about cold (on-column) injection , if it is part of a separate injector unit we talk about cold trap injection. A similar band compression effect may be achieved in a different way by leaving the first part of the capillary column uncoated (i.e. no stationary phase present). The solute band will then be compressed at the point where the stationary phase starts to be present in the column. This band compression technique is usually referred to by the unfortunate term retention gap [706]. [Pg.306]

Avoid the risk of cold zones in the combustion chamber by providing ... [Pg.166]

The submerged-flame technique developed by BASF represents the latest de> cIopment in autothermal processes. Within a liquid hydrocarbon, a flame creates a suf ciently high temperature in its vicinity to cause the formation of light products, tnduding acetylene. The gases are quendied in the cold zones of the liquid, and the carbon black formed is sent with the hydrocarbon to the burner. The reactor can operate undo pressure with any hydrocarbon oomponnd, without the substandal producdon of carbon black. The weak point of the device is the control of the burner, which is difficult to achieve due to the bi gas flow velocity (Fig. 5.13). [Pg.320]

Cold Zone This area is adjacent (and uphill and upwind) to the warm zone and is where decontaminated victims enter. As the victims enter this area, a more thorough triage is performed (including evaluation for secondary injuries), and victims are directed to treatment areas based on the severity and nature of illness or injury. Personal protective equipment is maintained in this area in case the wind changes or victims arrive who have been improperly decontaminated. [Pg.175]

During triage for mass casualty chemical incidents, what are the differences in the triage activities in the hot, warm, and cold zones ... [Pg.176]

Transfer pafienf fo clean backboard and exit into Cold Zone for rapid assessmenf, friage, and assignment to a treatment area. [Pg.514]

These differences may reflect mainly the effort expended on the two methods, rather than their intrinsic merits. The FTT work was done before the meteorite results became available, and so many of the non-protein amino acids simply were not looked for. Also, both syntheses persumably involve the same two steps (Miller et al., 1976) formation of unstable intermediates at high T, and rapid quenching and hydrolysis of the reaction products. The standard Miller-Urey flask, with its small spark zone and large liquid phase, is an optimal configuration for this purpose, in contrast to the FTT flask, where the hot and cold zones are in reverse ratio. If the intermediates and reaction paths indeed are similar (Miller et al., 1976), then it should be possible to improve yields in the FTT synthesis merely by changing the configuration of the apparatus, to provide a larger cold zone and faster quench. [Pg.15]


See other pages where Cold zones is mentioned: [Pg.118]    [Pg.136]    [Pg.418]    [Pg.212]    [Pg.474]    [Pg.262]    [Pg.40]    [Pg.88]    [Pg.88]    [Pg.349]    [Pg.410]    [Pg.36]    [Pg.37]    [Pg.81]    [Pg.44]    [Pg.564]    [Pg.174]    [Pg.506]    [Pg.349]    [Pg.262]    [Pg.143]    [Pg.192]    [Pg.184]   
See also in sourсe #XX -- [ Pg.20 ]




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Characteristics of Cold Seep Fluids at Subduction Zones

Cold zone dimension

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