Sulfate size distribution

Figure 13.7 Normalized sulfate size distributions measured in Los Angeles. The smaller mode dp 0.2 jum) wa.s observed during periods of low relative liuinidity, in the absence of morning fog. The larger mode (dp 0.5 rm) occurred on high-humidity days and was observed more frequently. (After Hering and Friedlandcr. 19S2.)...

Aluminum chlorohydrate [12359-72-7] Al2(OH) Gl 2H20 is a PAG product of specific composition, having r = 2.5. Aluminum chlorohydrate is used in antiperspirants regulated by the U.S. Food and Dmg Administration (FDA). Solutions sold for FDA-approved use are colorless in appearance, have 23—24% Al as AI2O2, and low levels of iron (<50 ppm), sulfate (<0.025 %), metals (Ga, Mg, Na <10 ppm), and heavy metals (as Pb <10 ppm). The pH of these solutions at 25°G is about 3.8—4.0. Typically, solutions at 25°G have specific gravities from 1.33 to 1.35 and viscosities from 40 to 60 mPa-s(=cps). Aluminum chlorohydrate [12042-91 -0] is also available in dry form with different particle-size distributions. 

For a given set of assumptions it is possible to calculate the characteristic curves for the product from the ciystaUizer when it is operated at various levels of fines removal as characterized by Lj. This has been done for an ammonium sulfate crystalhzer in Fig. 18-63. Also shown in that figure is the actual size distribution obtained. In calculating theoretic size distributions in accordance with the Eq. (18-41), it is... 

Strong acids are able to donate protons to a reactant and to take them back. Into this class fall the common acids, aluminum hahdes, and boron trifluoride. Also acid in nature are silica, alumina, alumi-nosihcates, metal sulfates and phosphates, and sulfonated ion exchange resins. They can transfer protons to hydrocarbons acting as weak bases. Zeolites are dehydrated aluminosilicates with small pores of narrow size distribution, to which is due their highly selective action since only molecules small enough to enter the pores can reacl . 

This paper summarizes part of the results of an investigation designed to characterize the aerodynamic size distributions of natural radioactivity and to evaluate the results in the context of sulfate distributions and recent advances in the understanding of aerosol growth mechanisms. This paper, while emphasizing our results on Pb-212 and Pb-214, also summarizes our initial data for longer-lived radionuclides. 

The experimental results reported in this paper demonstrate the ability of a flat-bottom hydrocyclone to separate the coarse fraction of ammonium sulfate crystals from a slurry which contains crystals of a wide size range. It appears that the grade efficiency curve, which predicts the probability of a particle reporting to the underflow of the cyclone as a function of size, can be adjusted by a change in the underflow diameter of the hydrocyclone. These two observations lead to the suggestion to use hydrocyclone separation to reduce the crystal size distribution which is produced in crystallisers, whilst using a variable underflow diameter as an additional input for process control. 

As we have seen in our earlier discussion of the size distribution of tropospheric particles, the chemical components are not generally distributed equally among all sizes but, rather, tend to be found in specific size ranges characteristic of their source. Generally, the smallest ultrafine particles are produced by homogeneous nucleation and hence tend to contain secondary species such as sulfate and likely organics (see Section A.2). Particles in the Aitken nuclei range are produced... 

Figure 9.35 shows a typical set of mass size distributions for total suspended particles (TSP), Na, Cl, Al, V, NO-, S04, and NH4 at Chichi in the Ogasawara (Bonin) Islands, about 1000 km southeast of the main island of Japan (Yoshizumi and Asakuno, 1986). As expected for a marine site such as this, Na and Cl from sea salt predominate, and both the TSP and Na and Cl components peak in the coarse particle range. Al is also found primarily in the larger particles and is attributed to a contribution from soil dust. On the other hand, vanadium, non-sea salt sulfate (nss-S04 ), and ammonium are primarily in the fine particles. The vanadium levels are extremely low and likely reflect long-range transport of an air mass containing the products of combustion of fuel oil, which contains V because it is likely associated with a combustion source, it would be expected in the fine particle mode, consistent with Fig. 9.35. 

FIGURE 9.36 Average size distributions for sulfate in continental and marine aerosol. AM M, is the fraction of the total mass of sulfate (Mr) found in each particle size range (adapted from Milford and Davidson, 1987). 

Li-Jones, X., and J. M. Prospero, Variations in the Size Distribution of Non-Sea-Salt Sulfate Aerosol in the Marine Boundary Layer at Barbados Impact of African Dust, J. Geophys. Res., 103, 16073-16084 (1998). 

Rivera-Carpio, C. A., C. E. Corrigan, T. Novakov, J. E. Penner, C. F. Rogers, and J. C. Chow, Derivation of Contributions of Sulfate and Carbonaceous Aerosols to Cloud Condensation Nuclei from Mass Size Distributions, . /. Geophys. Res., 101, 19483-19493 (1996). 

Wilson, J. C M. R. Stolzenburg, W. E. Clark, M. Loewenstein, G. V. Ferry, K. R. Chan, and K. K. Kelly, Stratospheric Sulfate Aerosol in and near the Northern Hemisphere Polar Vortex The Morphology of the Sulfate Layer, Multimodal Size Distributions, and the Effect of Denitrification, J. Geophys. Res., 97, 7997-8013 (1992). 

Fig. 1.1.9 Particle size distribution curves obtained by light scattering for two different aluminum hydrous oxide sols prepared by aging at 98°C for 30 h solutions containing 5 X I0-4 and I X 10" mol dm--1 Al2(S04)j, respectively (solid lines). Dashed lines show the corresponding size distributions of the same sols after all sulfate ions in the particles had been exchanged for hydroxyl groups.

Emulsifier is not a necessary component for emulsion polymerization if ihe following conditions are satisfied The particles are formed by homogeneous nucleation mechanism, and the particles are stabilized by factor(s) olher than emulsifier. As to the latter, the sulfate end group that is the residue of persulfate initiator serves for stabilization of dispersion via interparticle electrorepulsive force (20). When the stabilization mechanism works well, a small number of particles grow during polymerization without aggregation, keeping the size distribution narrow. Finally stable, monodisperse, anionic particles are obtained. 

Deionized water (720 g), sodium lauryl sulfate (4.3 g), dioctanoyl peroxide (40 g), and acetone (133 g) were emulsified using an ultrasonic probe for 10 minutes. The step 1 polystyrene seed (48.0 g seed, 578 g latex) was added to the emulsion together with lauryl sulfate (0.8 g) and acetone (29.6 g). The mixture was transferred to a flask and left to agitate at approximately 25°C for 48 hours. Acetone was then removed and the solution added to a 5-liter double-walled glass reactor. The temperature was increased to 40°C while styrene (336 g) and divinyl benzene (0.88 g) were added drop-wise over approximately 60 minutes. After 4 hours the mixture was treated with deionized water (1200 g), potassium iodide (1.28 g), and polyvinyl pyrrolidone (18.48 g) with the temperature increased to 70°C. The polymerization continued for 6 hours at 70°C and 1 hour at 90°C. Styrene-based oligomer particles with a diameter of 1.7 pm and with a narrow size distribution were obtained. 

Figure 7.22 Microstructure of acidified mixed emulsions (20 vol% oil, 0.5 wt% sodium caseinate) containing different concentrations of dextran sulfate (DS). Samples were prepared at pH = 6 in 20 mM imidazole buffer and acidified to pH = 2 by addition of HCl. Emulsions were diluted 1 10 in 20 mM imidazole buffer before visualization by differential interference contrast microscopy (A) no added DS (B) 0.1 wt% DS (C) 0.5 wt% DS (D) 1 wt% DS. Particle-size distributions of the diluted emulsions determined by light-scattering (Mastersizer) are superimposed on the micrographs, with horizontal axial labels indicating the particle diameter (in pm). Reproduced with permission from Jourdain et al. (2008).

Figure 2. Pore size distributions in titania-sulfate aerogels before (a) and after calcination (b).

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