Abstract

Glucose and fructose are widely available and renewable resources. They were used to prepare acetic acid (AA) under the catalysis of potassium acetate (KAc) by thermogravimetric analysis (TGA) and pyrolysis coupled with gas chromatography and mass spectrometry (Py-GC/MS). The TGA result showed that the KAc addition lowered the glucose’s thermal decomposition temperatures (about 30 °C for initial decomposition temperature and 40 °C for maximum mass loss rate temperature), implying its promotion of glucose’s decomposition. The Py-GC/MS tests illustrated that the KAc addition significantly altered the composition and distribution of hexose pyrolysis products. The maximum yield of AA was 52.1% for the in situ catalytic pyrolysis of glucose/KAc (1:0.25 wt/wt) mixtures at 350 °C for 30 s. Under the same conditions, the AA yield obtained from fructose was 48% and it increased with the increasing amount of KAc. When the ratio reached to 1:1, the yield was 53.6%. In comparison, a study of in situ and on-line catalytic methods showed that KAc can not only catalyze the primary cracking of glucose, but also catalyze the cracking of a secondary pyrolysis stream. KAc plays roles in both physical heat transfer and chemical catalysis.

Highlights

  • Acetic acid (AA) is a widely used bulk chemical in industrial production, with an annual output exceeding 10 million tons [1,2]

  • The addition of the KAc to the glucose made the thermogravimetric (TG) and differential thermogravimetric (DTG) profiles shift to the lower temperature region

  • Both the glucose and the KAc DTG curves had a distinct peak corresponding to the decomposition and no dehydration peaks indicated that the material were not damp again after overnight drying

Read more

Summary

Introduction

Acetic acid (AA) is a widely used bulk chemical in industrial production, with an annual output exceeding 10 million tons [1,2]. AA is consumed to produce acetic anhydride, vinyl acetate monomer [3], cellulose acetate [4] and calcium magnesium acetate which is called low corrosive and environmentally friendly deicer [5,6,7]. It can be used as a green solvent for the production of pure terephthalic acid in the food industry [8]. There are several processes for AA production, such as microbial fermentation, methanol carbonylation, hydrocarbons (ethylene, acetaldehyde, butane and naphtha) oxidation, synthesis gas preparation, methyl formate isomerization, hydrothermal oxidation and pyrolysis. Ethylene oxidation has by-products [16]

Methods
Results
Conclusion
Full Text
Paper version not known

Talk to us

Join us for a 30 min session where you can share your feedback and ask us any queries you have

Schedule a call

Disclaimer: All third-party content on this website/platform is and will remain the property of their respective owners and is provided on "as is" basis without any warranties, express or implied. Use of third-party content does not indicate any affiliation, sponsorship with or endorsement by them. Any references to third-party content is to identify the corresponding services and shall be considered fair use under The CopyrightLaw.