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Pores uniform distributions

A porous structure with small pores uniformly distributed can be achieved chemically by evolution of gas with the mixed slurry followed by stabilization of the bubble structure. The gas must be formed by reaction between two evenly and finely dispersed substances. Also, the rate of reaction must be slow, particularly immediately after mixing, so that the gas-producing substances can be incorporated properly before a significant amount of gas has evolved. Otherwise, much of the gas is lost during the mixing step. Mixtures of carbonates with acids such as dolomite and sulfuric acid have been used. Stabilization of the mixture to prevent bubbles from rising to the surface can be... [Pg.341]

The pore-size distribution and the nature of the pores in catalyst supports and hence the catalysts derived from them are important properties that significantly affect catalyst performance (16). In most cases, catalyst designers prefer an open-pore stmcture, that is, pores that have more than one opening, and a pore size as uniform as possible in order to obtain maximum utilization of the available pore volume. This can be achieved by careful choice of raw materials and processing conditions. [Pg.194]

When the catalyst is expensive, the inaccessible internal surface is a liabihty, and in every case it makes for a larger reactor size. A more or less uniform pore diameter is desirable, but this is practically reahz-able only with molecular sieves. Those pellets that are extrudates of compacted masses of smaller particles have bimodal pore size distributions, between the particles and inside them. Micropores have diameters of 10 to 100 A, macropores of 1,000 to 10,000 A. The macropores provide rapid mass transfer into the interstices that lead to the micropores where the reaction takes place. [Pg.2095]

A narrow pore size distribution is essential to HOPC. To separate polymer samples with various average molecular weights, users need to prepare columns packed with porous materials of a uniform but different pore size, e.g., 10, 13, 18, and 24 nm. In contrast, a broader pore size distribution is common in a SEC column. A need to analyze a wide range of molecular weights (over many decades) by a single set of columns has spread the use of these columns. [Pg.618]

The porous materials that offer the narrowest possible pore size distribution are those that have cylindrical pores of uniform diameter penetrating the entire medium without branching. Branching gives polymer molecules in the junctions extra conformational entropy. An agglomerate of tiny pieces of these porous materials, interlaced with larger voids (much larger than the pore size), should also be chosen. [Pg.618]

The pores of tire separating membrane are to be most uniformly distributed and of minimum size to avoid deposition of metallic particles and thus electronic bridging. One distinguishes between macroporous and microporous separators, the latter having to show pore diameters below I micron (/urn ), i.e., below one-thousandth of a millimeter. Thus the risk of metal particle deposition and subsequent shorting is quite low, since active materials in storage batteries usually have particle diameters of several microns. [Pg.247]

The small pore size and the uniform distribution result in capillary forces which should allow wicking heights and thus battery heights of up to 30 cm. Due to the cavities required for gas transfer and under the effect of gravity, the electrolyte forms a filling profile, i.e., fewer cavities remain at the bottom than at the top. Therefore with absorptive glass mats a rather flat battery... [Pg.279]

The advantage of sol-gel technology is the ability to produce a highly pure y-alumina and zirconia membrane at medium temperatures, about 700 °C, with a uniform pore size distribution in a thin film. However, the membrane is sensitive to heat treatment, resulting in cracking on the film layer. A successful crack-free product was produced, but it needed special care and time for suitable heat curing. Only y-alumina membrane have the disadvantage of poor chemical and thermal stability. [Pg.387]

Gel filtration chromatography has been extensively used to determine pore-size distributions of polymeric gels (in particle form). These models generally do not consider details of the shape of the pores, but rather they may consider a distribution of effective average pore sizes. Rodbard [326,327] reviews the various models for pore-size distributions. These include the uniform-pore models of Porath, Squire, and Ostrowski discussed earlier, the Gaussian pore distribution and its approximation developed by Ackers and Henn [3,155,156], the log-normal distribution, and the logistic distribution. [Pg.549]

Membranes with a relatively uniform pore size distribution throughout the thickness of the membrane are referred to as symmetric or homogeneous membranes. Others may be formed with tight skin layers on the top or on both the top and bottom of the membrane surfaces. These are referred to as asymmetric or nonhomogeneous membranes. In addition, membranes can be cast on top of each other to form a composite membrane. [Pg.38]

One of the early questions raised on TUD-1 dealt with its pore structure did it have intersecting or nonintersecting pores At the University of Utrecht, one conclusive characterization was carried out with a silica TUD-1 with Pt inserted, which was analyzed by 3-D TEM (transmission electron microscopy) (9). The Pt anchors (not shown) were used as a focal point for maintaining the xyz orientation. As shown in Figure 41.2, the TUD-1 is clearly amorphous. While not quantitatively measured for this sample, the pores appear rather uniform, consistent with all porosimetry measurements on TUD-1 showing narrow pore size distributions. [Pg.368]

When submitting a carbonate rock to the flov of an acidic solution, the attack, most of the time, leads to the preferential grovth of large pores. The dissolution of the rock is not uniform, and the final pore size distribution is much broader than the original one. This fact has been recognized and described in detail more than fifteen years ago (4j 5). Macroscopic pores, which are the end result of such an unstable attack, have received the name of wormholes. [Pg.609]

This relation is plotted as curve Bin Figure 12.11. Smith (66) has shown that the same limiting forms for are observed using the concept of effective dififusivities and spherical catalyst pellets. Curve B indicates that, for fast reactions on catalyst surfaces where the poisoned sites are uniformly distributed over the pore surface, the apparent activity of the catalyst declines much less rapidly than for the case where catalyst effectiveness factors approach unity. Under these circumstances, the catalyst effectiveness factors are considerably less than unity, and the effects of the portion of the poison adsorbed near the closed end of the pore are not as apparent as in the earlier case for small hr. With poisoning, the Thiele modulus hp decreases, and the reaction merely penetrates deeper into the pore. [Pg.465]

Mesoporous silicas have characteristics of high specific surface areas and pores with defined dimensions and uniform distribution. These features make mesoporous systems ideal candidates as host materials to guest bio-molecules. Protein stability may be enhanced due to reduced autolysis in the case of protease enzymes, and more generally reduced protein aggregation, as a result of the separation of the molecules adsorbed on the surface. [Pg.11]

As described before, the pore size of porous material ranges widely from atomic size to millimeter order. Different pore sizes are required for different applications of porous materials. Most porous materials do not have uniform pores. Pore size distribution is also an important property. Narrow pore size distribution, i.e., uniform pore size, is required for instance for filters and bioreactor beds. Mercury porosimetry and gas adsorption methods are commonly used to measure pores size and pores distribution. [Pg.358]

Figure 1.6 Top Low-temperature nitrogen adsorption ( ) and desorption (x) isotherms measured on a calcined SBA-15 mesoporous silica solid prepared using an EO20PO70EO20 block copolymer [54]. Bottom Pore size distribution derived from the adsorption isotherm reported at the top [54]. A high surface area (850 m2/g), a uniform distribution of cylindrical nanopores (diameter —90 A), and a large pore volume (1.17 cm3/g) were all estimated from these data. These properties make this material suitable for use as support in the preparation of high-surface-area solid catalysts. (Reproduced with permission from The American Chemical Society.)... Figure 1.6 Top Low-temperature nitrogen adsorption ( ) and desorption (x) isotherms measured on a calcined SBA-15 mesoporous silica solid prepared using an EO20PO70EO20 block copolymer [54]. Bottom Pore size distribution derived from the adsorption isotherm reported at the top [54]. A high surface area (850 m2/g), a uniform distribution of cylindrical nanopores (diameter —90 A), and a large pore volume (1.17 cm3/g) were all estimated from these data. These properties make this material suitable for use as support in the preparation of high-surface-area solid catalysts. (Reproduced with permission from The American Chemical Society.)...
Textural mesoporosity is a feature that is quite frequently found in materials consisting of particles with sizes on the nanometer scale. For such materials, the voids in between the particles form a quasi-pore system. The dimensions of the voids are in the nanometer range. However, the particles themselves are typically dense bodies without an intrinsic porosity. This type of material is quite frequently found in catalysis, e.g., oxidic catalyst supports, but will not be dealt with in the present chapter. Here, we will learn that some materials possess a structural porosity with pore sizes in the mesopore range (2 to 50 nm). The pore sizes of these materials are tunable and the pore size distribution of a given material is typically uniform and very narrow. The dimensions of the pores and the easy control of their pore sizes make these materials very promising candidates for catalytic applications. The present chapter will describe these rather novel classes of mesoporous silica and carbon materials, and discuss their structural and catalytic properties. [Pg.118]

Figure 9.25 Models of granules of monodisperse particles characteristic psds (pore size distributions) are given below (a) uniform packing (b) bidisperse packing of aggregates of particles of similar sizes (c) same as (b) but the size of aggregates vary in a wide range. Figure 9.25 Models of granules of monodisperse particles characteristic psds (pore size distributions) are given below (a) uniform packing (b) bidisperse packing of aggregates of particles of similar sizes (c) same as (b) but the size of aggregates vary in a wide range.
The randomly distributed sheet clearly exhibits areas of low and high density but it still remains a good target and a unique reference structure in making paper. The small scale non-uniformities of paper structure are particularly important in their influence on pore size distribution and the distribution of areal mass density, and both of these properties have an influence on mechanical and other properties of the final sheet. [Pg.52]

Pore diameters of the PS layer formed under a given set of conditions have a distinct distribution. Normal, log-normal, bimodal, fractal, and non-uniform distributions have been found for PS formed under different conditions.26,29,60,88,89,90,91... [Pg.167]

For an unconsolidated porous medium with uniform pore size distribution, the ratio of VJHa approaches its maximum value much more rapidly than that found in a medium where pore size distribution is nonuniform, leading to the significant variation of water saturation in the contaminated zone. [Pg.195]


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