Abstract
A new process for the production of 1,5-pentanediol (1,5-PDO) from biomass-derived furfural is studied. In this process, furfural is converted to 1,5-PDO in a high overall yield (80%) over inexpensive catalysts via multiple steps involving hydrogenation, dehydration, hydration, and hydrogenation subsequently. To effectively recycle H2 as well as recover 1,5-PDO, detailed separation subsystems have been designed and integrated with reaction subsystems. Furthermore, a pioneer plant analysis is performed to estimate the risk on the cost growth and plant performance shortfalls. The integrated process leads to a minimum selling price of $1973 ton-1 for 1,5-PDO, which suggests that it could be a promising approach for converting biomass into oxygenated commodity chemicals, which are difficult to produce from petroleum-derived feedstocks. The sensitivity analysis also identifies that the most important economic parameters for the process include the furfural feedstock price and plant size.
Original language | English (US) |
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Pages (from-to) | 4699-4706 |
Number of pages | 8 |
Journal | ACS Sustainable Chemistry and Engineering |
Volume | 5 |
Issue number | 6 |
DOIs | |
State | Published - Jun 5 2017 |
Externally published | Yes |
All Science Journal Classification (ASJC) codes
- General Chemistry
- Environmental Chemistry
- General Chemical Engineering
- Renewable Energy, Sustainability and the Environment
Keywords
- 1,5-Pentanediol
- Biorefinery
- Catalytic conversion
- Furfural
- Pioneer plant analysis
- Process design
- Technoeconomic analysis