4.7 Article

Process synthesis and analysis of green plastic monomer production from cellulose

Journal

JOURNAL OF CLEANER PRODUCTION
Volume 277, Issue -, Pages -

Publisher

ELSEVIER SCI LTD
DOI: 10.1016/j.jclepro.2020.124072

Keywords

Process design; Technoeconomic; Heat exchanger network; Polyethylene 2,5-furandicarboxylate; Gamma-valerolactone; Ion exchanger

Funding

  1. National Research Foundation of Korea (NRF) - Korean government (MSIT) [2018R1C1B6009074]
  2. C1 Gas Refinery Program through the National Research Foundation of Korea - Ministry of Science ICT and Future Planning [2015M3D3A1A01064929]
  3. National Research Foundation of Korea [2018R1C1B6009074] Funding Source: Korea Institute of Science & Technology Information (KISTI), National Science & Technology Information Service (NTIS)

Ask authors/readers for more resources

As a renewable building block, 2,5-furandicarboxylic acid (FDCA) is a potentially viable alternative to petro-based terephthalic acid (TPA). For the commercialization of FDCA production, economically feasible process development is crucial. In this study, we design a new catalytic conversion process for the production of the green plastic monomer (FDCA) and evaluate the economic feasibility of the process. In the proposed process, the FDCA is produced from cellulose using a bio-based green solvent composed of gamma-valerolactone (GVL) and H2O via three-step conversion involving cellulose hydrolysis, glucose dehydration and 5-hydroxymethylfurfural (HMF) oxidation subsequently. For the efficient recovery of solvents and products, the separation subsystem is designed and integrated with the conversion process. Moreover, to improve energy efficiency, a heat exchanger network combined with a heat pump is designed. The new process increases the FDCA productivity by 17% and reduces the total capital investment by 52.6% after optimization. Furthermore, this proposed process leads to the minimum selling price (MSP) of $1366/t for FDCA, which suggests that the proposed process for bio-based FDCA production is a promising approach to substitute petro-based TPA ($1445/t). The sensitivity analysis identifies that the main cost drivers are a feedstock price, steam price and discount rate, which should be investigated for the further improvement of the economics of the process. (C) 2020 Elsevier Ltd. All rights reserved.

Authors

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

Reviews

Primary Rating

4.7
Not enough ratings

Secondary Ratings

Novelty
-
Significance
-
Scientific rigor
-
Rate this paper

Recommended

No Data Available
No Data Available