4.8 Article

Bio-based process for the catalytic production of ethyl levulinate from cellulose

Journal

APPLIED ENERGY
Volume 300, Issue -, Pages -

Publisher

ELSEVIER SCI LTD
DOI: 10.1016/j.apenergy.2021.117430

Keywords

Catalytic process; Techno-economics; Energy integration; Process design; Ethanol; Ethyl levulinate

Funding

  1. Basic Science Research Program through the National Research Foundation of Korea (NRF) - Ministry of Education [2019R1I1A3A01061118]
  2. Technology Development Program of the National Research Foundation (NRF) - Ministry of Science and ICT [2020M1A2A2080858]
  3. National Research Foundation of Korea [2019R1I1A3A01061118, 2020M1A2A2080858] Funding Source: Korea Institute of Science & Technology Information (KISTI), National Science & Technology Information Service (NTIS)

Ask authors/readers for more resources

The study presents a bio-based process for catalytic conversion of cellulose to ethyl levulinate and analyzes its techno-economic feasibility. Experimental results show that the process can achieve high ethyl levulinate yields but requires complex recycling procedures for used catalyst and solvent.
This paper presents a bio-based process for the catalytic conversion of cellulose to ethyl levulinate and an analysis of its techno-economic feasibility. The said bio-based process relies as major feedstock on cellulose, which can be derived from lignocellulosic biomass. cellulose is converted to ethyl levulinate via a homogeneous catalytic reaction whereby dilute sulfuric acid in combination with Al salts is the catalyst and ethanol is the solvent and reactant. This approach affords high ethyl levulinate yields but requires complex procedures for used catalyst and solvent recycling. Based on experimental results on the homogeneous catalytic reaction and vapor-liquid equilibrium separation in the previous studies, a simulation was conducted that included process design, energy integration, and economic analysis. Results from this simulation indicated the proposed bio-based process to afford a minimum selling price of US$ 2,830 per ton of ethyl levulinate, which was highly dependent on an off-site supply of heating energy required for ethanol purification.(1)

Authors

I am an author on this paper
Click your name to claim this paper and add it to your profile.

Reviews

Primary Rating

4.8
Not enough ratings

Secondary Ratings

Novelty
-
Significance
-
Scientific rigor
-
Rate this paper

Recommended

No Data Available
No Data Available