Fly ash has been converted to zeolite using alkali fusion followed by hydrothermal treatment. The synthesis conditions were optimized to obtain highest conversion of fly ash to X-type zeolite. The prepared catalyst has demonstrated good efficiency in catalytic cracking of pure components, like n-Heptane, as well as heavy gas oil. The cracking activity of synthesized catalyst showed comparable activity with 13X zeolite and FCC catalyst collected from Bharat Petroleum Corporation Ltd., India. The activity of the synthesized catalyst has been tested for lkylation of phenol. The prepared catalyst has been found to be superior to the commercially available catalyst like 13X and H-Beta. The cracking and alkylation reactions were carried out in a fixed bed down flow reactor and also in batch reactor. Kinetic models were developed for both for cracking and alkylation reactions and kinetic parameters and adsorption constants were estimated using a non-linear regression algorithm. The outcome of the present study is very much promising in utilizing a waste material into a commercial commodity and also to protect environmental pollution to some extent.
Les informations fournies dans la section « Synopsis » peuvent faire référence à une autre édition de ce titre.
Fly ash has been converted to zeolite using alkali fusion followed by hydrothermal treatment. The synthesis conditions were optimized to obtain highest conversion of fly ash to X-type zeolite. The prepared catalyst has demonstrated good efficiency in catalytic cracking of pure components, like n-Heptane, as well as heavy gas oil. The cracking activity of synthesized catalyst showed comparable activity with 13X zeolite and FCC catalyst collected from Bharat Petroleum Corporation Ltd., India. The activity of the synthesized catalyst has been tested for lkylation of phenol. The prepared catalyst has been found to be superior to the commercially available catalyst like 13X and H-Beta. The cracking and alkylation reactions were carried out in a fixed bed down flow reactor and also in batch reactor. Kinetic models were developed for both for cracking and alkylation reactions and kinetic parameters and adsorption constants were estimated using a non-linear regression algorithm. The outcome of the present study is very much promising in utilizing a waste material into a commercial commodity and also to protect environmental pollution to some extent.
Dr. Keka Ojha, Associate Professor of the Department of Petroleum Engineering, ISM, Dhanbad, India has nearly 8 years of research and teaching experience. Dr. Ojha, a graduate in Chemical Engineering (Hons.) from Jadavpur University, has received her Masters and Doctoral degree from IIT, Kharagpur, India in Chemical Engineering.
Les informations fournies dans la section « A propos du livre » peuvent faire référence à une autre édition de ce titre.
Vendeur : BuchWeltWeit Ludwig Meier e.K., Bergisch Gladbach, Allemagne
Taschenbuch. Etat : Neu. This item is printed on demand - it takes 3-4 days longer - Neuware -Fly ash has been converted to zeolite using alkali fusion followed by hydrothermal treatment. The synthesis conditions were optimized to obtain highest conversion of fly ash to X-type zeolite. The prepared catalyst has demonstrated good efficiency in catalytic cracking of pure components, like n-Heptane, as well as heavy gas oil. The cracking activity of synthesized catalyst showed comparable activity with 13X zeolite and FCC catalyst collected from Bharat Petroleum Corporation Ltd., India. The activity of the synthesized catalyst has been tested for lkylation of phenol. The prepared catalyst has been found to be superior to the commercially available catalyst like 13X and H-Beta. The cracking and alkylation reactions were carried out in a fixed bed down flow reactor and also in batch reactor. Kinetic models were developed for both for cracking and alkylation reactions and kinetic parameters and adsorption constants were estimated using a non-linear regression algorithm. The outcome of the present study is very much promising in utilizing a waste material into a commercial commodity and also to protect environmental pollution to some extent. 220 pp. Englisch. N° de réf. du vendeur 9783843358491
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Etat : New. Dieser Artikel ist ein Print on Demand Artikel und wird nach Ihrer Bestellung fuer Sie gedruckt. Autor/Autorin: Ojha KekaDr. Keka Ojha, Associate Professor of the Department of Petroleum Engineering, ISM, Dhanbad, India has nearly 8 years of research and teaching experience. Dr. Ojha, a graduate in Chemical Engineering (Hons.) from Jadavpur U. N° de réf. du vendeur 5465826
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Taschenbuch. Etat : Neu. Utilization of Fly ash as catalyst for Cracking and Alkylation | Synthesis and Characterization of zeolite from Fly ash for Cracking of n-Heptane and Alkylation of Phenol | Keka Ojha | Taschenbuch | 220 S. | Englisch | 2010 | LAP LAMBERT Academic Publishing | EAN 9783843358491 | Verantwortliche Person für die EU: preigu GmbH & Co. KG, Lengericher Landstr. 19, 49078 Osnabrück, mail[at]preigu[dot]de | Anbieter: preigu. N° de réf. du vendeur 107232921
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Taschenbuch. Etat : Neu. This item is printed on demand - Print on Demand Titel. Neuware -Fly ash has been converted to zeolite using alkali fusion followed by hydrothermal treatment. The synthesis conditions were optimized to obtain highest conversion of fly ash to X-type zeolite. The prepared catalyst has demonstrated good efficiency in catalytic cracking of pure components, like n-Heptane, as well as heavy gas oil. The cracking activity of synthesized catalyst showed comparable activity with 13X zeolite and FCC catalyst collected from Bharat Petroleum Corporation Ltd., India. The activity of the synthesized catalyst has been tested for lkylation of phenol. The prepared catalyst has been found to be superior to the commercially available catalyst like 13X and H-Beta. The cracking and alkylation reactions were carried out in a fixed bed down flow reactor and also in batch reactor. Kinetic models were developed for both for cracking and alkylation reactions and kinetic parameters and adsorption constants were estimated using a non-linear regression algorithm. The outcome of the present study is very much promising in utilizing a waste material into a commercial commodity and also to protect environmental pollution to some extent.VDM Verlag, Dudweiler Landstraße 99, 66123 Saarbrücken 220 pp. Englisch. N° de réf. du vendeur 9783843358491
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Taschenbuch. Etat : Neu. nach der Bestellung gedruckt Neuware - Printed after ordering - Fly ash has been converted to zeolite using alkali fusion followed by hydrothermal treatment. The synthesis conditions were optimized to obtain highest conversion of fly ash to X-type zeolite. The prepared catalyst has demonstrated good efficiency in catalytic cracking of pure components, like n-Heptane, as well as heavy gas oil. The cracking activity of synthesized catalyst showed comparable activity with 13X zeolite and FCC catalyst collected from Bharat Petroleum Corporation Ltd., India. The activity of the synthesized catalyst has been tested for lkylation of phenol. The prepared catalyst has been found to be superior to the commercially available catalyst like 13X and H-Beta. The cracking and alkylation reactions were carried out in a fixed bed down flow reactor and also in batch reactor. Kinetic models were developed for both for cracking and alkylation reactions and kinetic parameters and adsorption constants were estimated using a non-linear regression algorithm. The outcome of the present study is very much promising in utilizing a waste material into a commercial commodity and also to protect environmental pollution to some extent. N° de réf. du vendeur 9783843358491
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