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Conversion of acetone and mixed ketones to hydrocarbons using HZSM-5 catalyst in the carboxylate platform. | LitMetric

Conversion of acetone and mixed ketones to hydrocarbons using HZSM-5 catalyst in the carboxylate platform.

PLoS One

Department of Chemical Engineering, Texas A&M University, College Station, Texas, United States of America.

Published: November 2022

AI Article Synopsis

  • The study examines the production of hydrocarbons from two feeds: reagent-grade acetone and mixed ketones derived from lignocellulosic biomass using a catalyst called HZSM-5.
  • In experiments with acetone, varying temperatures and weight hourly space velocity (WHSV) were tested, revealing 100% conversion at high temperatures with aromatic products centered on C8, while lower temperatures produced less conversion and C9 compounds.
  • For mixed ketones, the results showed a maximum conversion of 40%, but the catalyst experienced significant deactivation, leading to fluctuations in product concentrations over time.

Article Abstract

In this study, two different feeds were treated to produce hydrocarbons: (1) reagent-grade acetone, and (2) mixed ketones obtained from lignocellulosic biomass via the carboxylate platform. Acetone and mixed ketones underwent catalytic self-condensation over HZSM-5. For acetone, HZSM-5(80) was used, and the experiments were conducted in two sets: (1) vary temperature (305-415°C) at P = 101 kPa (abs) and weight hourly space velocity (WHSV) = 1.3 h-1; (2) vary WHSV (1.3-7.9 h-1) at T = 350 and 415°C, and P = 101 kPa (abs). For acetone over HZSM-5(280), the experiments were conducted in two sets: (1) vary WHSV (1.3-6.5 h-1) at T = 415°C, and P = 101 kPa (abs); and (2) vary WHSV (1.3-11.8 h-1) at P = 790 kPa (abs) and T = 415°C. For mixed ketones, HZSM-5(280) was used at WHSV = 1.9 h-1, T = 430-590°C, and P = 101 kPa (abs). For acetone at higher temperatures, the conversion was 100% and the liquid products were aromatics centered on C8. At low temperatures, conversion was less and the carbon liquid distribution was centered on C9 (mainly mesitylene). For mixed ketones, catalyst deactivation was higher causing product concentrations to change over time, and the highest conversion reached was 40%.

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Source
http://www.ncbi.nlm.nih.gov/pmc/articles/PMC9678301PMC
http://journals.plos.org/plosone/article?id=10.1371/journal.pone.0277184PLOS

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