Abstract
Among various utilization technologies for soapstock, catalytic pyrolysis for hydrocarbon-rich bio-oil production demonstrates promising potential. However, it currently suffers from drawbacks such as low selectivity of target products, which limits its large-scale application. This study developed a microwave-assisted in-situ catalytic pyrolysis system coupled with SiC for oil-tea camellia soapstock (OTCS) upgrading and addressed the issue of slow heating rates during the microwave-assisted pyrolysis of OTCS alone, which stem from fluctuations in microwave absorption capacity. Furthermore, the system was optimized through the application of various catalysts to screen for those yielding high-yield, high-quality bio-oil. Results showed that bio-oil yield reached 64.50 wt% with a microwave power of 800 W and a HY/OTCS mass ratio of 9/10. Aromatics content increased from 26.68 % under non-catalytic to 70.69 %, while oxygen-containing compounds content decreased from 21.38 % under non-catalytic to 7.13 %. The selectivity for aromatic hydrocarbons in the bio-oil was significantly improved without a substantial decline in the overall bio-oil yield, thereby effectively enhancing its value. This study provides a theoretical basis and technical paradigm for the targeted production of high-value aromatics from soapstock, and promotes the utilization of by-products from grain and oil industry.
| Original language | English (US) |
|---|---|
| Article number | 137559 |
| Journal | Fuel |
| Volume | 407 |
| DOIs | |
| State | Published - Mar 1 2026 |
Bibliographical note
Publisher Copyright:© 2025 Elsevier Ltd.
Keywords
- Catalytic pyrolysis
- Hydrocarbon-rich bio-oil
- Microwave-driven
- SiC heat carrier
- Soapstock
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