Design and optimization of bio-oil co-processing with vacuum gas oil in a refinery

被引：20
|
作者：
Wu, Le [1 ,2 ]
Wang, Yuqi [1 ,2 ]
Zheng, Lan [1 ,2 ]
Shi, Meirong [3 ]
Li, Jingying [1 ]
机构：
[1] Northwest Univ, Sch Chem Engn, Xian 710069, Peoples R China
[2] Shaanxi Prov Inst Energy Resource & Chem Engn, Xian 710069, Peoples R China
[3] Shanxi Inst Trade & Commerce, Sch Pharm, Xian 712046, Shaanxi, Peoples R China
来源：
ENERGY CONVERSION AND MANAGEMENT | 2019年 / 195卷
关键词：
Bio-oil; Vacuum gas oil; Co-processing; Superstructure; Integration; CATALYTIC PYROLYSIS OIL; HYDROCARBON BIOREFINERY; BIOMASS PYROLYSIS; FUEL PRODUCTION; CRACKING; FEEDSTOCK; BIOCRUDE; BIOFUELS; QUALITY; RAW;
D O I：
10.1016/j.enconman.2019.05.041
中图分类号：
O414.1 [热力学];
学科分类号：
摘要：
The prices of the bio-diesel and bio-gasoline are normally significantly high when compared to the petroleum-derived fuels. The co-processing of bio-oil and vacuum gas oil in a fluid catalytic cracker (FCC) has been proposed to utilize existing refinery infrastructures while lowering bio-fuel prices. Nonetheless, the integration of the bio-oil production and the existing refinery remains unknown. In this work, a superstructure model is proposed to design and optimize the co-processing process by selecting the optimal biomass feedstock and the bio-oil production process (fast pyrolysis or catalytic pyrolysis). Furthermore, the impacts of the FCC processing capability and bio-oil co-processing ratio on the economics as well as the selection of bio-oil production process are also investigated. As revealed by the results of two scenarios, pulpwood is the optimal biomass feedstock and the fast pyrolysis ought to be selected for producing bio-oil when its co-processing ratio and the FCC processing capability are both relatively high.
引用
收藏
页码：620 / 629
页数：10
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