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Droplet drying

For materials that dry without crust fonimtion into solid spherical particles, the final powder mean dimeter. Dp, can be determined by the initial mean droplet diameter, D, and the solid content of the liquid as follows [14]  [Pg.315]

Chapter 8 Other Ceramic Powder Fabrication Processes [Pg.316]

FIGURE 8.6 Frames of a motion crust formation and final structure [Pg.317]

FIGURE 8.7 Temperature around an evaporating drop. Redravm from Ranz and Marshall [15]. [Pg.317]


Most of the AHoy 600 outer diameter tube corrosion has occurred in the region of the upper tubesheet near the open lane, ie, an untubed lane across the middle of the steam generator (16,17). The steam carries entrained droplets of water through the open lane to the upper tubesheet region where the droplets dry out and concentrate the chemicals. Long tube inserts have been used to sleeve tubes in this region where wall defects have been detected. [Pg.194]

The accuracy of VPD-TXRF depends largely on the reliability of the reference material (cf Sect. 4.1.1.3) and on the reproducibility of the droplet drying procedure (Fig. 4.17) [4.75, 4.76]. Mass absorption sets the upper limit of reliable analyses to lO atoms cm [4.77]. [Pg.192]

Print buffers 3X SSC, 3X SSC + 50% DMSO, and 3X SSC + 1.5 M betaine were evaluated at 40, 60, and 80% RH for spot intensity, spot diameter, intraspot variation, and CV (Figure 4.35). The reductions in quill drop volumes and droplet drying times were measured by video microscope and the quill reservoir volume changes determined by weight. In summary, "Solvent evaporation from the print buffer reservoir is the major factor responsible for the variations in the transfer of fluid to fhe slide surface."... [Pg.129]

Two models can explain the events that take place as the droplets dry. One was proposed by Dole and coworkers and elaborated by Rollgen and coworkers [7] and it is described as the charge residue mechanism (CRM). According to this theory, the ions detected in the MS are the charged species that remain after the complete evaporation of the solvent from the droplet. The ion evaporation model affirms that, as the droplet radius gets lower than approximately 10 nm, the emission of the solvated ions in the gas phase occurs directly from the droplet [8,9]. Neither of the two is fully accepted by the scientific community. It is likely that both mechanisms contribute to the generation of ions in the gas phase. They both take place at atmospheric pressure and room temperature, and this avoids thermal decomposition of the analytes and allows a more efficient desolvation of the droplets, compared to that under vacuum systems. In Figure 8.1, a schematic of the ionization process is described. [Pg.235]

N. Abuaf, F.W. Staub, Drying of liquid-solid slurry droplets, Drying 86 Proc. 5th Int. Drying Symp. 1 (1987) 227-248. [Pg.191]

Evaporation. As a liquid droplet is formed of a volatile solvent and a polymer, evaporation of the solvent will lead to polymer beads entrapping the active ingredients. Spray drying consists of spraying a (aqueous) polymer solution and droplet drying. Emulsification of polymer volatile organic solvent in water followed by solvent removal is called the solvent evaporation method. [Pg.31]

A drying film of ink can be considered as behaving like a very large droplet. Just as a hemispherical droplet dries to leave a circular coffee... [Pg.65]

Spray drying involves three fundamental steps (1) atomization, (2) droplet drying, and (3) gas-droplet mixing. Each of these steps will be discussed in the following sections. The particles produced by spray drying are sometimes spherical and other times in the shape of a punctured spherical shell. The distribution of internal stnicture and chemistry including binder are not uniform inside a spray dried particle because it dries from the outside, first bringing impurities finm the center of the droplet to the surface where they are crystallized out or left behind when the solvent evaporates. [Pg.309]

The mechanism of the anionic depression has been the subject of many investigations. It is generally beheved that as the aerosol droplet dries up in the preheating zone or in the flame itself, a compound is formed between the metal and the anion which interferes with or retards the... [Pg.30]

The solution or suspension to be dried is sprayed into a hot air stream and circulated through a chamber. The dried product may be carried out to cyclone or bag separators or may fall to the bottom of the drying chamber and be expelled through a valve. The chambers are normally cylindrical with a conical bottom although proportions vary widely. The process can be divided into four sections atomization of the fluid, mixing of the droplets, drying, and finally removal and collection of the dry particles. [Pg.3893]

Performing a series of droplet tracking calculations using the results from the CFD simulation, a representative droplet drying experience can be developed from the example shown in Figure 15. The early droplet temperature profile with time is shown in Figure 16 in which the initial decline, warm-up and constant rate equilibrium are evident. The falling rate period was not modeled hence the particle temperature is seen to rise to the local gas field temperature once evaporation has ceased. Note the time scale for this series of events is less then 6 milliseconds. [Pg.248]

Matrix Polymer matrix with dispersed oil or flavour droplets Dry product Limited (oxidative) stability of encapsulated flavour Flavour can be loaded in empty particles Tunable release... [Pg.404]

The above information is all that is required to perform a preliminary sizing on a spray dryer. The temperature limit of the product is given at 170°F. Using 160 F as the outlet temperature of the dryer should allow us the safety necessary so as not to exceed the temperature limit of the dry powder (product). The fact that we get evaporative cooling while drying the spherically shaped droplets to a similarly shaped powder allows us to use an inlet temperature of about 320°F. Thus the temperature difference (AT) is 160°F. This is the primary driving force in motivating the water to leave the product due to the enormous difference in saturation equilibrium between the wet droplet/dry powder and the very hot dry air. [Pg.749]

Furuta T, Tsujimoto S, Okazaki M, Toei R. 1984. Effect of drying on retention of ethanol in maltodextrin solution during drying of a single droplet. Drying Technology 2 311-327. [Pg.36]

Verhey JGP. 1973. Vacuole formation in spray-dried powder particles. 3. Atomization and droplet drying. Netherlands Milk and Dairy Journal 27 3-18. [Pg.40]

If the spray point is located too high, droplets dry completely before contacting the bed (excessive fmes/no agglomerates). [Pg.1001]

Main heat and mass transfer between droplets and drying medium takes place in the drying chamber. The drying chamber designs are directly related to the results of droplets drying. [Pg.55]

The following diffusion equation can be used to simulate a single droplet drying (falling rate period) in a hot moving airflow ... [Pg.219]

By the type of modeling methodology, the published theoretical models of droplet drying kinetics can be subdivided into the following categories (1) models based on semiempirical... [Pg.228]


See other pages where Droplet drying is mentioned: [Pg.131]    [Pg.761]    [Pg.197]    [Pg.338]    [Pg.70]    [Pg.168]    [Pg.315]    [Pg.322]    [Pg.325]    [Pg.325]    [Pg.640]    [Pg.32]    [Pg.2575]    [Pg.249]    [Pg.101]    [Pg.151]    [Pg.441]    [Pg.121]    [Pg.8]    [Pg.47]    [Pg.54]    [Pg.60]    [Pg.132]    [Pg.132]    [Pg.225]    [Pg.227]   
See also in sourсe #XX -- [ Pg.312 , Pg.319 , Pg.320 , Pg.321 , Pg.322 , Pg.323 , Pg.324 , Pg.325 , Pg.326 , Pg.327 , Pg.328 , Pg.329 , Pg.330 ]

See also in sourсe #XX -- [ Pg.273 ]




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