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Industrial adsorbents zeolites

The price of zeolites varies considerably depending on the apphcation. The typical price of catalysts in the United States varies from about US 3 /kg for FCC to about US 20/kg for specialty catalysts, adsorbents from about US 5-9/ kg, up to tens of dollars per kilogram for specialty adsorbents and about US 2/ kg for detergents. Natural zeolites in bulk applications sell for US 0.04—0.25/kg and in industrial adsorbent applications for US 1.50-3.50/kg [22]. [Pg.17]

The principal types of industrial adsorbent can be divided into amorphous and the crystalline types. The former includes activated carbon, silica gel, and activated alumina the latter includes zeolites and their aluminum phosphate, AIPO4 (or ALPO), analogs. Yang (2003) wrote that, since the invention of synthetic zeolites in 1959, adsorption has become a key separation tool in the chemical, petrochemical, and pharmaceutical industries. Adsorptive separation of different molecules can be achieved by three mechanisms equilibrium adsorption differences, diffusion kinetics differences. [Pg.321]

The hydrophobic nature of the activated carbons is best suited for the solvent vapor recovery applications because most industrial waste gas streams containing organic solvents are saturated with water vapor. Activated carbons can retain a large fraction of their dry adsorption capacities for organic compounds in presence of high humidity. Table 22.3 shows a few examples of this behawor [22]. Most polar adsorbents (zeolites, alumina, and silica gels) will not be effective for this appHcation. [Pg.572]

Keywords Adsorption theories isotherm data adsorbents zeolites activated carbons industrial applications. [Pg.977]

CO2, and in hydrocarbon adsorption and separation. Adsorption-based separation is an important process for hydrocarbon mixtures in the petrochemical industry. While zeolite-based molecular sieves have been successfully applied for such commercial applications since the middle of the past century, " MMOFs offer distinct advantages, thanks to their adjustable pore dimensions, unique pore geometries, and functionalized pore surfaces. In this chapter, we give a concise summary of the various aspects of hydrocarbon and alcohol adsorption and separation using MMOFs as the adsorbent. [Pg.321]

ZeoHte catalysts and adsorbents are widely accepted in industry. Commercial adsorbents based on synthetic aluminosihcates zeolite A and X became available in 1948 [4]. Zeolite Y as FCC catalyst became commercially available in 1964 [5]. [Pg.212]

Many procedures that are used in zeolite catalyst and adsorbent manufacture are common to other manufactured products. The unit operahons and equipment that are used can therefore be found throughout the catalyst and adsorbent manufacturing industries. There are a number of books and monographs that outhne equipment and manufacturing procedures that are relevant to zeoHte catalysts and adsorbents [65-68]. [Pg.68]

Another application for adsorption of metal impurities is in the nuclear power industry. Radioactive cesium is one of the compounds that is difficult to remove from radioactive waste. This is because ordinary resins and zeolites do not effectively adsorb radioactive cesium. In 1997, lONSlV lE-911 crystalline silicotitan-ate (CST) ion exchangers were developed and effectively used to clean up radioactive wastes in the Melton Valley tanks at Oak Ridge [268, 269], CST was discovered [270] by researchers at Sandia National Laboratories and Texas A M University, with commercial manufacture carried out by UOP. [Pg.191]

As documented in Chapter 5, zeolites are very powerful adsorbents used to separate many products from industrial process steams. In many cases, adsorption is the only separation tool when other conventional separation techniques such as distillation, extraction, membranes, crystallization and absorption are not applicable. For example, adsorption is the only process that can separate a mixture of C10-C14 olefins from a mixture of C10-C14 hydrocarbons. It has also been found that in certain processes, adsorption has many technological and economical advantages over conventional processes. This was seen, for example, when the separation of m-xylene from other Cg-aromatics by the HF-BF3 extraction process was replaced by adsorption using the UOP MX Sorbex process. Although zeolite separations have many advantages, there are some disadvantages such as complexity in the separation chemistry and the need to recover and recycle desorbents. [Pg.203]

Adsorptive separation is a powerful technology in industrial separations. In many cases, adsorption is the only technology available to separate products from industrial process streams when other conventional separation tools fail, such as distillation, absorption, membrane, crystallization and extraction. Itis also demonstrated that zeolites are unique as an adsorbent in adsorptive separation processes. This is because zeolites are crystalline soUds that are composed of many framework structures. Zeolites also have uniform pore openings, ion exchange abiUty and a variety of chemical compositions and crystal particle sizes. With the features mentioned, the degree of zeoUte adsorption is almost infinite. It is also noted that because of the unique characteristics of zeoHtes, such as various pore openings, chemical compositions and structures, many adsorption mechanisms are in existence and are practiced commercially. [Pg.225]

The two adsorbent chambers contain the zeolitic adsorbent, the liquid xylenes and p-diethylbenzene desorbent. Proper loading of the adsorbent into the large diameter vessels in industrial production plants is of critical importance to maximize adsorbent mass in the fixed vessel volume and not generate low and high density areas within the adsorbent bed. Density inconsistencies could adversely affect liquid flow distribution and thereby have a detrimental effect on the performance of the process. Adsorbent loading methods are a matter of proprietary know how of the technology licensors. However, Seko has published a paper on the practical matters involved in an actual problem case [20]. [Pg.236]

This is the first book to offer a practical overview of zeolites and their commercial applications. Each chapter is written by a globally recognized and acclaimed leader in the field. The book is organized into three parts. The first part discusses the history and chemistry of zeolites, the second part focuses on separation processes and the third part explores zeolites in the field of catalysis. AH three parts are tied together by their focus on the unique properties of zeolites that allow them to function in different capabilities as an adsorbent, a membrane and a catalyst. Each of the chapters also discusses the impact of zeolites within the industry. [Pg.625]

We define zeolites with Si02/Al203 molar ratio > 5 as high silica zeolites. These, typically exemplified by ZSM-5, play an important role as industrial catalysts. Studies to apply them as hydrophobic adsorbents have also been conducted. [Pg.37]

The conversion of methanol to hydrocarbons (MTHC) on acidic zeolites is of industrial interest for the production of gasoline or light olefins (see also Section X). Upon adsorption and conversion of methanol on calcined zeolites in the H-form, various adsorbate complexes are formed on the catalyst surface. Identification of these surface complexes significantly improves the understanding of the reaction mechanism. As demonstrated in Table 3, methanol, dimethyl ether (DME), and methoxy groups influence in a characteristic manner the quadrupole parameters of the framework Al atoms in the local structure of bridging OH groups. NMR spectroscopy of these framework atoms under reaction conditions, therefore, helps to identify the nature of surface complexes formed. [Pg.189]

Sorption capacity is one of the major properties used for industrial applications of zeolites. H. Lee reviews the aspects of zeolites used as adsorbents. The other papers in the section deal with the theory of sorption and diffusion in porous systems, the variation of sorption behavior upon modification, and the variation of crystal parameters upon adsorption. NMR and ESR studies of sorption complexes are reported. H. Resing reviews the mobility of adsorbed species in zeolites studied by NMR. [Pg.8]

New applications of zeolite adsorption developed recently for separation and purification processes are reviewed. Major commercial processes are discussed in areas of hydrocarbon separation, drying gases and liquids, separation and purification of industrial streams, pollution control, and nonregenerative applications. Special emphasis is placed on important commercial processes and potentially important applications. Important properties of zeolite adsorbents for these applications are adsorption capacity and selectivity, adsorption and desorption rate, physical strength and attrition resistance, low catalytic activity, thermal-hydrothermal and chemical stabilityy and particle size and shape. Apparent bulk density is important because it is related to adsorptive capacity per unit volume and to the rate of adsorption-desorption. However, more important factors controlling the raJtes are crystal size and macropore size distribution. [Pg.311]

Vne of the major industrial applications of zeolites is in the area of ad-sorption processes. Zeolite adsorbents are not only the most important adsorbents today, but their importance is increasing, mainly because of the following unique adsorptive properties (a) selective adsorption of molecules based on molecular dimensions, (b) highly preferential adsorption of polar molecules, (c) highly hydrophilic surface, and (d) variation of properties by ion exchange. [Pg.311]

Contrary to catalytic applications, zeolite adsorbents are mostly applied in a fixed-bed operation. A number of columns packed with zeolite adsorbent(s) are interconnected with an automatic valve system to facilitate a continuous flow of the industrial stream being processed. Each bed, however, goes through a stepwise cyclic operation, and during each cycle the adsorbed molecules in the zeolite bed are desorbed by raising the bed temperature, lowering the bed pressure, displacing the adsorbate with another adsorbate, or combination. [Pg.311]

Major industrial adsorption processes using zeolite adsorbents may be classified as follows (I) hydrocarbon separation processes, (II) drying gases and liquids, (III) separation and purification of industrial streams, (IV) pollution control applications, and (V) nonregenerative applications. Some important commercial processes in each of these areas are discussed briefly. [Pg.312]


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Adsorbents zeolitic

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