Membrane preparation metal membranes

A novel method of preparing metal membranes with nearly suaight pores has been described by Masuda et al. [1993]. Basically it involves a two-step molding process (Figure 3.15). A porous anodized aluminum structure without the aluminum substrate removed is used as a template and the pores of the anodic alumina is filled with a monomer such as methylmethacrylate (MMA) and an initiator (e.g., benzoyl peroxide)... 

Because membranes appHcable to diverse separation problems are often made by the same general techniques, classification by end use appHcation or preparation method is difficult. The first part of this section is, therefore, organized by membrane stmcture preparation methods are described for symmetrical membranes, asymmetric membranes, ceramic and metal membranes, and Hquid membranes. The production of hollow-fine fiber membranes and membrane modules is then covered. Symmetrical membranes have a uniform stmcture throughout such membranes can be either dense films or microporous. 

The permeability tests for alkali metal ions in the aqueous solution were also conducted. When an aqueous salt solution moves to cell 2 through the membrane from cell 1, the apparent diffusion coefficient of the salt D can be deduced from a relationship among the cell volumes Vj and V2, the solution concentration cx and c2, the thickness of membrane, and time t6 . In Table 12, permeabilities of potassium chloride and sodium chloride through the 67 membrane prepared by the casting polymerization technique from the monomer solution in THF or DMSO are compared with each other and with that the permeability through Visking dialyzer tubing. The... 

The chemical composihons of the zeolites such as Si/Al ratio and the type of cation can significantly affect the performance of the zeolite/polymer mixed-matrix membranes. MiUer and coworkers discovered that low silica-to-alumina molar ratio non-zeolitic smaU-pore molecular sieves could be properly dispersed within a continuous polymer phase to form a mixed-matrix membrane without defects. The resulting mixed-matrix membranes exhibited more than 10% increase in selectivity relative to the corresponding pure polymer membranes for CO2/CH4, O2/N2 and CO2/N2 separations [48]. Recently, Li and coworkers proposed a new ion exchange treatment approach to change the physical and chemical adsorption properties of the penetrants in the zeolites that are used as the dispersed phase in the mixed-matrix membranes [56]. It was demonstrated that mixed-matrix membranes prepared from the AgA or CuA zeolite and polyethersulfone showed increased CO2/CH4 selectivity compared to the neat polyethersulfone membrane. They proposed that the selectivity enhancement is due to the reversible reaction between CO2 and the noble metal ions in zeolite A and the formation of a 7i-bonded complex. 

A.G. Boricha and Z. Murthy, Acrylonitrile butadiene styrene/chitosan blend membranes Preparation, characterization and performance for the separation of heavy metals, J. Membr. Sci., 339(l-2) 239-249, September 2009. 

In this chapter membrane preparation techniques are organized by membrane structure isotropic membranes, anisotropic membranes, ceramic and metal membranes, and liquid membranes. Isotropic membranes have a uniform composition and structure throughout such membranes can be porous or dense. Anisotropic (or asymmetric) membranes, on the other hand, consist of a number of layers each with different structures and permeabilities. A typical anisotropic membrane has a relatively dense, thin surface layer supported on an open, much thicker micro-porous substrate. The surface layer performs the separation and is the principal barrier to flow through the membrane. The open support layer provides mechanical strength. Ceramic and metal membranes can be either isotropic or anisotropic. 

Recently, attempts have been made to reduce the cost of palladium metal membranes by preparing composite membranes. In these membranes a thin selective palladium layer is deposited onto a microporous ceramic, polymer or base metal layer [19-21], The palladium layer is applied by electrolysis coating, vacuum sputtering or chemical vapor deposition. This work is still at the bench scale. 

Preparation of Pt-TiOx/Pd membranes. It was also desirable to prepare metalloceramic membranes in which the catalytic activity of the ceramic phase was enhanced through the addition of a noble metal. The very low surface area of the titania films prepared as described above made them difficult to impregnate with adequate dispersion by traditional incipient wetness techniques. Instead, finely ground titania (>200 mesh) was impregnated with platinum via the incipient wetness method with a chloroplatinic acid solution. This powder was then sprinkled onto the surface of a freshly dipped membrane, which was dried and heat treated as described. These materials were activated before use at 350°C in hydrogen for three hours. 

To conclude this section, it is necessary to state that Pd and Pd-based membranes are currently the membranes with the highest hydrogen permeability and selectivity. However, the cost, availability, their mechanical and thermal stabilities, poisoning, and carbon deposition problems have made the large-scale industrial application of these dense metal membranes difficult, even when prepared in a composite configuration [26,29,33-37],... 

Compared to the 6 mol-% La-doped membranes, calcium and gadolinium-doped membranes showed larger pores and more pore growth during SASRA treatment. This indicates that the stabilising effect of the latter metal ions is not of the same quality as that of lanthanum. These findings could be of interest, however, for the preparation of membranes with specific pore-... 

By itself a subject of study, metallic yam used in the past comes in a number of varieties that reflect the level of technology and trade of the time. A majority of metallic threads has been made into yarn by cutting prepared metallic material into strips that were then wound around a core thread of silk or linen. The metallic materials used were either gold or silver leaf adhered to membrane, parchment, leather, or paper or plain soft metal. Membrane is adversely affected by water and... 

The reaction mixture was composed of 50 p.L of membrane preparation, 10 mM Hepes-Tris buffer (pH 6.8), 1.5 mM MgQ2, 1.5 mM EGTA, and 0.1 mM thiamine triphosphate in a total volume of 100 fiL. After 15 minutes of incubation at 25°C, the reaction was stopped by addition of 500 fiL of 6% trichloroacetic acid. The supemate obtained by centrifugation was extracted with 4 volumes of diethyl ether. The thiamine derivatives were transformed into fluorescent thiochromes by the addition of 50 fiL of oxidant [4.3 mJW K3Fe(CN)6 in 15% NaOH] to 80 fiL of sample. Thiamine diphosphatase activity was minimized by using magnesium as the metal and EGTA to chelate calcium. 

The manufacture of dense metal membranes or thin films can be effected by a number of processes casting/rolling, vapor deposition by physical and chemical means, electroplating (or electroforming) and electroless plating. By far, casting in combination with rolling is the predominant preparation and fabrication technique. It is noted that many of these processes have been demonstrated with palladium and its alloys because of their low oxidation propensity. Preparation of dense metal membranes is summarized in some detail as follows. 

Examples of common metal oxide membranes prepared by sol-gel process... 

Some selective double alkoxides have been synthesized and can be utilized to prepare mixed metal oxide membranes. Preparation and stabilities of double or multiple metal alkoxides are sometimes challenging. Aluminum alkoxides are particularly interesting as they are reactive with other metal alkoxides [Bradley et al., 1978]. Some alkoxides... 

Porous metal membranes similarly can be prepared by this technique of heat treatment followed by leaching with a strong acid, base or hydrogen peroxide [Croopnick and Scruggs, 1986]. 

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