This monograph describes the production of hydrocarbons from acetone and isopropanol produced by the MixAlco process. The MixAlco process has two types of products: acetone and isopropanol. The effect of the temperature, weight hourly space velocity (WHSV), type of catalyst, feed composition, and pressure are studied. For the isopropanol reaction, the following conditions were used: HZSM-5 (280), 1 atm, 300–410°C, and 0.5–11.5 h–1, respectively. The temperature and WHSV affect the average carbon number of the reaction products. A product similar to commercial gasoline was obtained at T = 320 °C and WHSV= 1.3 to 2.7 h–1. For the acetone reaction, the following conditions were used: HZSM-5 with silica alumina ratio (Si/Al) 80 and 280 mol silica/mol alumina, 1–7.8 atm, 305–415°C, 1.3–11.8 h–1, and hydrogen acetone ratio 0–1 mol H2 /mol acetone. The conversion on HZSM-5 (80) was higher than HZSM-5 (280). For acetone, the effect of high pressure and co-feeding hydrogen was also studied. The Appendixes contain the product distribution for all the experiments and concentration profiles of commercial gasolines.
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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.In January 2010, he started his PhD program in the same Department.
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Taschenbuch. Condition: Neu. This item is printed on demand - it takes 3-4 days longer - Neuware -This monograph describes the production of hydrocarbons from acetone and isopropanol produced by the MixAlco process. The MixAlco process has two types of products: acetone and isopropanol. The effect of the temperature, weight hourly space velocity (WHSV), type of catalyst, feed composition, and pressure are studied. For the isopropanol reaction, the following conditions were used: HZSM-5 (280), 1 atm, 300-410°C, and 0.5-11.5 h-1, respectively. The temperature and WHSV affect the average carbon number of the reaction products. A product similar to commercial gasoline was obtained at T = 320 °C and WHSV= 1.3 to 2.7 h-1. For the acetone reaction, the following conditions were used: HZSM-5 with silica alumina ratio (Si/Al) 80 and 280 mol silica/mol alumina, 1-7.8 atm, 305-415°C, 1.3-11.8 h-1, and hydrogen acetone ratio 0-1 mol H2 /mol acetone. The conversion on HZSM-5 (80) was higher than HZSM-5 (280). For acetone, the effect of high pressure and co-feeding hydrogen was also studied. The Appendixes contain the product distribution for all the experiments and concentration profiles of commercial gasolines. 152 pp. Englisch. Seller Inventory # 9783847373308
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Taschenbuch. Condition: Neu. nach der Bestellung gedruckt Neuware - Printed after ordering - This monograph describes the production of hydrocarbons from acetone and isopropanol produced by the MixAlco process. The MixAlco process has two types of products: acetone and isopropanol. The effect of the temperature, weight hourly space velocity (WHSV), type of catalyst, feed composition, and pressure are studied. For the isopropanol reaction, the following conditions were used: HZSM-5 (280), 1 atm, 300-410°C, and 0.5-11.5 h-1, respectively. The temperature and WHSV affect the average carbon number of the reaction products. A product similar to commercial gasoline was obtained at T = 320 °C and WHSV= 1.3 to 2.7 h-1. For the acetone reaction, the following conditions were used: HZSM-5 with silica alumina ratio (Si/Al) 80 and 280 mol silica/mol alumina, 1-7.8 atm, 305-415°C, 1.3-11.8 h-1, and hydrogen acetone ratio 0-1 mol H2 /mol acetone. The conversion on HZSM-5 (80) was higher than HZSM-5 (280). For acetone, the effect of high pressure and co-feeding hydrogen was also studied. The Appendixes contain the product distribution for all the experiments and concentration profiles of commercial gasolines. Seller Inventory # 9783847373308
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