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Efficiency temperature

The process illustrates the use of mechanical refrigeration in its high-efficiency temperature range the maximum use of compression energy because of its high efficiency and the use of turboexpansion at a low temperature—its Carnot efficiency is best at low temperatures, especially because it permits large use of the efficient pressure effect. [Pg.52]

When selecting a system to remove particulate from a gas stream, many choices concerning equipment can be made. The selection could be made on the basis of cost, gas pressure drop, efficiency, temperature, resistance, etc. Table 29-3 summarizes these factors for comparative purposes. The tabular values must not be considered absolute because great variations occur between types and manufacturers. No table is a substitute for a qualified consulting engineer or a reputable manufacturer s catalog. [Pg.473]

For counter-current flow of the fluids through the unit with sensible heat transfer only, this is the most efficient temperature driving force with the largest temperature cross in the unit. The temperature of the outlet of the hot stream can be cooler than the outlet temperature of the cold stream, see Figure 10-29 ... [Pg.54]

Reducer R XNOjmaX (%) T Width at half conversion Tso (°C) Tioo (°C) Efficiency (temperature integrated... [Pg.303]

Only a few microwave reactors equipped with efficient temperature control systems for safe microwave synthesis at laboratory scale are currently available on the market. These systems lead to reproducible operating conditions. [Pg.23]

Although microwave-heated organic reactions can be smoothly conducted in open vessels, it is often of interest to work with closed systems, especially if superheating and high-pressure conditions are desired. When working under pressure it is strongly recommended to use reactors equipped with efficient temperature feedback coupled to the power control and/or to use pressure-relief devices in the reaction vessels to avoid vessel rupture. Another potential hazard is the formation of electric arcs in the cavity [2], Closed vessels can be sealed under an inert gas atmosphere to reduce the risk of explosions. [Pg.380]

Energy efficiency. Temperature gradients are steady state and take place in space rather than in time, reducing the need for the expensive heating and cooling cycles common in batch equipment. [Pg.240]

Bio-Logic Instrument and Laboratories (Meylan, France) manufactures an SFM-3 stopped-flow instrument (Fig. 4.17) that consists of three independent drive syringes driven by stepping motors, two mixers and a delay line, three observation windows, replaceable cuvettes, no stop-syringes, and efficient temperature regulation. At maximum flow rate, the minimum dead times range from 1.0 to 4.9 ms for fluorescence detection and 1.3 ms for transmittance. Currently, the Bio-Logic MOS-IOOO optical system employs fluorescence or absorbance detection, which is not suitable... [Pg.92]

Let us first restrict to the simpler and more frequently encountered case that the feed mixture consists of vapors of a single component B in the carrier gas A. The optimum device, both at ambient and elevated pressure, will then be a saturator which contains component B in the solid or liquid state (Fig. 2). On its way through the saturator, the carrier gas A is loaded with vapors of B. Since its vapor pressure depends exponentially on the temperature, the saturator must be thoroughly thermostated. An externally thermostated water or oil bath circulating through a jacket around the saturator is often the best solution. If temperatures above ca. 200 °C are required, a saturator surrounded by a stirred bath of molten salt with an efficient temperature control can be used alternatively. [Pg.403]

Distillation is a veiy common method for purifying liquids. Atmospheric distillation (general distillation), vacuum distillation, and steam distillation are the three common methods of distillation. Atmospheric distillation takes place at atmospheric pressure, which means the distillation apparatus is open to the air. Vacuum distillation utilizes reduced pressure to distill a liquid at lower temperature. Vacuum distillation is commonly used to distill liquids, which tend to decompose at their atmospheric boiling points. Vacuum distillation is also used to conveniently distill liquids with relatively high boiling points at a much more efficient temperature. Steam distillation is similar to atmospheric distillation, but steam is used to promote volatility. Steam distillation only works on liquids or solids, which are volatile with steam. [Pg.32]

The parameters that need special consideration for the successful coupling on an SFC to a CLND are restrictor position, ozone generation, combustion efficiency (temperature and oxygen flow rate), and quenching. Each of these will be discussed in detail. [Pg.1547]

At the present time, all industrial plants operate in the vapor phase, although certain developments have been conducted to achieve the oxychlorinatkm of ethylene in the liquid phase, particularly by Kellogg. In this case, transformation takes place around 170 to 185 C at between 15 and 2.10 Pa absolute, in the presence of a catalyst system based on promoted cuprous and cupric chlorides, with more efficient temperature control by vaporization of part of the reaction medium and better performance, but with acid... [Pg.170]

Efficient temperature conditions for thermal treatment of the covering with heating wire have been set. [Pg.110]

The effects of fy, Fv, and FL on the temperature T are indirect and rather slow, while that of Ws is direct and faster. Therefore, from the 24 loop configurations of Table 23.1, only numbers 1, 3, 7, 9,14, and 18 look promising for efficient temperature control. [Pg.601]

The checkers recovered a 1 1 mixture of tetraester and d1ketone from two runs conducted for 2.5 hr. When the reflux time was extended to 6 hr, complete conversion to product was attained. The reaction progress was monitored by gas evolution (Note 14). Some variability of reaction times is probably attributable to differences in stirring efficiency, temperature gradients, and/or particle size of the crystalline starting material. [Pg.133]

Bimstock., J., Lux, A., Ammarm, M. et al. 2006. Novel materials and structures for highly-efficient, temperature-stable, and long-living AM OLED displays. SID Inti. Symp. Dig. Tech. Papers 37 1866. [Pg.507]

The electrodialysis process to make silica aquasols commercial electrodialysis units is technically feasible. The new variable temperature method allows to make very small particle size sols (4-6 nm) and concentrated small particle sols (7 nm) at higher, more efficient temperatures. Electrodialysis remains an attractive technical option for new plant an electrodialysis plant would cost less than a completely new ion exchange resin plant. Electrodialysis is an energy intensive process but it is essentially pollution-free and recovers substantial NaOH values for credit. Location of a plant in a low-cost power area could be attractive. Electrodialysis would also be a technical option in case environmental pressures require further reduction of sodium sulfate level in the silica sol waste of the ion exchange resin process. [Pg.100]


See other pages where Efficiency temperature is mentioned: [Pg.64]    [Pg.181]    [Pg.253]    [Pg.21]    [Pg.311]    [Pg.17]    [Pg.233]    [Pg.33]    [Pg.143]    [Pg.574]    [Pg.311]    [Pg.74]    [Pg.155]    [Pg.152]    [Pg.520]    [Pg.453]    [Pg.485]    [Pg.238]    [Pg.875]    [Pg.151]    [Pg.162]    [Pg.218]    [Pg.117]    [Pg.73]    [Pg.218]    [Pg.694]    [Pg.230]    [Pg.200]    [Pg.257]    [Pg.87]    [Pg.124]   
See also in sourсe #XX -- [ Pg.66 ]




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