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Condensation mode

Cmde helium (containing 50—70% helium, associated hydrogen and neon, 1—3% methane, and the balance nitrogen) can easily be obtained by minor enhancements to the nitrogen rejection unit, particularly with natural gases containing 0.5% or more helium. For example, by operating the double-column condenser in a partial condensation mode, a stream of uncondensed vapor at about 50% helium concentration can be obtained. This cmde helium stream can be fed directly to helium purification and Hquefaction units. [Pg.333]

Boilers and air heaters can be designed to operate in the condensing mode, that is, the outlet temperature of the products entering the flue can be at or close to the dewpoint. The usual design criteria for flues which attempt to avoid condensation are no longer applicable and it is necessary to incorporate additional features. These will include ... [Pg.271]

Condensed mode operation. To avoid accumulation of liquid in the reactor the dew point of the gas must be kept above reactor temperature. When operating in condensed mode, higher-boiling components in the recirculating gas are allowed to condense in the heat exchanger, and this liquid is fed back to the reactor where it evaporates. [Pg.284]

Similarly, by Schiff-base condensation reactions have been used to generate free cryptands from triamines and dicarbonyls in [2+3] condensation mode. These ligands react with silver(I) compounds to give dinuclear or trinuclear macrocyclic compounds where Ag Ag interactions may be present. Thus, with a small azacryptand a dinuclear complex with a short Ag- Ag distance (55) is found.498 With bigger azacryptand ligands also dinuclear complexes as (56) are achieved but without silver-silver interaction. 65,499-501 A heterobinuclear Ag1—Cu1 cryptate has also been... [Pg.934]

Hering and Friedlander (1982) made similar observations for particle sulfate and attributed the smallest mode (referred to as the condensation mode) to formation from gas-phase S02 oxidation and the larger modes (the droplet mode) to oxidation in the condensed phase. Meng and Seinfeld (1994) have shown that the droplet mode particles cannot arise from growth of the smaller, condensation mode particles and propose that the condensation mode particles are activated to form fog or cloud droplets, followed by chemical reactions and subsequent evaporation to form the droplet particles. [Pg.356]

The detail of their synthesis involving anionic, cationic, and free radical and condensation modes. [Pg.162]

Features - particles of growing polymer form in fluidized bed - catalyst residence time 2-4 hours - morphology and psd of catalyst are important - previously (pre-1990s) restricted in range of comonomer that could be used because of emergence of "condensed" mode operation, a wide range of comonomers may now be used... [Pg.94]

In the 1990s, an improvement for the gas phase process was developed called "condensed mode" operation of Unipol reactors (12). This technique greatly expanded capacity of gas phase reactors and product capability by making it more practical to use higher alpha-olefin comonomers such as octene-1. [Pg.94]

The plant has been commissioned and the first results on the performance are expected soon. Design data give an efficiency to power of 23 and 27 % respectively for extraction and condensation mode of operation while the overall plant efficiency is 73 and 39 % respectively. [Pg.23]

Power Section CHPMode See note 1 Condensing Mode... [Pg.839]

Note 1 For the pyrolysis case the power section is run in two modes Combined Heat and Power mode during the operation of the sugar mill to provide steam needed to supplement the mill s steam demand, and Condensing mode during the period when the mill is not in operation. ... [Pg.839]

FIGURE 1.13 Supe r-condensed mode of olefin polymerization. [Pg.26]

Fig. 4 Schematic illustration of the use of hydrophilic zeolite coating to change condensation mode from drop-wise without zeolite film (A) to film-wise with zeolite film (B). Fig. 4 Schematic illustration of the use of hydrophilic zeolite coating to change condensation mode from drop-wise without zeolite film (A) to film-wise with zeolite film (B).
The reactions of 5,10-methylene THF models with mononucleophiles mainly take place in 1 2 stoichiometry but in some highly functionalized systems an alternate 1 1 condensation mode of reaction prevails. The syntheses of various targets obtained through these reactions are elaborated. [Pg.169]

Processing of accumulation and coarse mode aerosols by clouds (Chapter 17) can also modify the concentration and composition of these modes. Aqueous-phase chemical reactions take place in cloud and fog droplets, and in aerosol particles at relative humidities approaching 100%. These reactions can lead to production of sulfate (Chapter 7) and after evaporation of water, a larger aerosol particle is left in the atmosphere. This transformation can lead to the formation of the condensation mode and the droplet mode (Hering and Friedlander 1982 John et al. 1990 Meng and Seinfeld 1994). [Pg.373]

Measurements of the urban aerosol mass distribution have shown that two distinct modes often exist in the 0.1 to 1.0 pm diameter range (Hering and Friedlander 1982 McMurry and Wilson 1983 Wall et al. 1988 John et al. 1990). These are referred to as the condensation mode (approximate aerodynamic diameter 0.2 pm) and the droplet mode (aerodynamic diameter around 0.7 pm). These two submicrometer mass distribution modes have also been observed in nonurban continental locations (McMurry and Wilson 1983 Hobbs et al. 1985 Radke et al. 1989). Hering and Friedlander (1982) and John et al. (1990) proposed that the larger mode could be the result of aqueous-phase chemical reactions. Meng and Seinfeld (1994) showed that growth of condensation mode particles by accretion of water vapor or by gas-phase or aerosol-phase sulfate production cannot explain existence of the droplet mode. Activation of condensation mode particles, formation of cloud/fog drops, followed by aqueous-phase chemistry, and droplet evaporation were shown to be a plausible mechanism for formation of the aerosol droplet mode. [Pg.802]

Measurements of the urban aerosol mass distribution have shown that two distinct modes often exist in the 0.1 to 1.0 fxm diameter range (Hering and Friedlander, 1982 McMurry and Wilson, 1983 Wall et al., 1988 John et al., 1990). These are referred to as the condensation mode (approximate aerodynamic diameter 0.2 /um) and the droplet mode... [Pg.820]

Film condensation is the prime condensation mode in distillation condensers. Dropwise condensation can help improve heat transfer, but it is seldom relied on. Fog formation constitutes an operation problem rather than a desirable condensation mode and is further discussed in Sec. 15.13. The following discussion focuses on film condensation. [Pg.468]

Vertical in-shell condensers. This is a common condensation mode in reboilers but not in overhead condensers. Vapor flows downward, (Figs. 15.1a, c, and 15.10a). The shell can be baffled (Fig. 15.10a), but often it is not for a single-component vapor. [Pg.471]

Horizontal in-tube condensers. Typical applications of this condensation mode are air condensers and horizontal condenser-reboilers. These condensers are often made in single-pass or U-tube arrangements, but multipass arrangements are also used. With multipass arrangements, successive passes should be below one another (291). Multipass condensation may be troublesome with multicomponent mixtures as described in the preceding section. [Pg.471]


See other pages where Condensation mode is mentioned: [Pg.399]    [Pg.788]    [Pg.32]    [Pg.25]    [Pg.280]    [Pg.2]    [Pg.341]    [Pg.349]    [Pg.13]    [Pg.21]    [Pg.164]    [Pg.270]    [Pg.26]    [Pg.1040]    [Pg.1012]    [Pg.3240]    [Pg.538]    [Pg.539]    [Pg.493]    [Pg.369]    [Pg.381]    [Pg.214]    [Pg.441]    [Pg.821]    [Pg.1344]    [Pg.489]    [Pg.102]   
See also in sourсe #XX -- [ Pg.14 ]

See also in sourсe #XX -- [ Pg.467 ]




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