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Oligomerization and Catalytic Ketonization in the Mixalco™ Process - Couverture souple

Taco-Vasquez, Sebastian; Holtzapple, Mark

 
9783659523694: Oligomerization and Catalytic Ketonization in the Mixalco™ Process
Couverture souple
ISBN 10 : 3659523690 ISBN 13 : 9783659523694
Editeur : LAP LAMBERT Academic Publishing, 2014

Synopsis

This research describes the zeolite use in the oligomerization and catalytic ketonization steps of the MixAlco™ process. In this book, the following six products associated with the MixAlco™ process were studied: acetic acid, mixed acids, acetone, mixed ketones, isopropanol, and mixed alcohols. The effect of the temperature (T), weight hourly space velocity (WHSV), type of catalyst, feed composition, and pressure (P) were studied. For the isopropanol and mixed alcohol reactions, the following conditions were used: HZSM-5 (280, moles of silica per mole of alumina = 280), T = 300–510°C, and P = 101, 5000, and 8000 kPa. Medium-molecular-weight olefins (1-hexene, 1-octene and 1-decene) were dimerized using Beta (25) zeolite catalyst in a batch reactor. For the catalytic ketonization of acetic acid and mixed acids, the following conditions were used: ZrO2 catalyst, T = 300–410°C. Acetic acid conversion was 100% at low WHSV and temperatures over 400°C. For mixed acids, maximum conversion was 95%.This study describes the pilot plant and reports results from an 11-month production campaign transforming paper and chicken manure into gasoline and jet fuel.

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Présentation de l'éditeur

This research describes the zeolite use in the oligomerization and catalytic ketonization steps of the MixAlco™ process. In this book, the following six products associated with the MixAlco™ process were studied: acetic acid, mixed acids, acetone, mixed ketones, isopropanol, and mixed alcohols. The effect of the temperature (T), weight hourly space velocity (WHSV), type of catalyst, feed composition, and pressure (P) were studied. For the isopropanol and mixed alcohol reactions, the following conditions were used: HZSM-5 (280, moles of silica per mole of alumina = 280), T = 300–510°C, and P = 101, 5000, and 8000 kPa. Medium-molecular-weight olefins (1-hexene, 1-octene and 1-decene) were dimerized using Beta (25) zeolite catalyst in a batch reactor. For the catalytic ketonization of acetic acid and mixed acids, the following conditions were used: ZrO2 catalyst, T = 300–410°C. Acetic acid conversion was 100% at low WHSV and temperatures over 400°C. For mixed acids, maximum conversion was 95%.This study describes the pilot plant and reports results from an 11-month production campaign transforming paper and chicken manure into gasoline and jet fuel.

Biographie de l'auteur

Sebastian Taco Vasquez received a B.S. in chemical engineering from Escuela Politecnica Nacional , Quito Ecuador in February 2007. In August 2007, he started his M.S. in the Department of Chemical Engineering at Texas A&M University, receiving his degree in December 2009. He continued his PhD in the same department, obtaining his degree in 2013.

Les informations fournies dans la section « A propos du livre » peuvent faire référence à une autre édition de ce titre.

Éditeur
LAP LAMBERT Academic Publishing
Date d'édition
2014
Langue
anglais
ISBN 10 
3659523690
ISBN 13 
9783659523694
Reliure
Broché
Nombre de pages
264
Coordonnées du fabricant
non disponible
Personne responsable
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