Comparative Techno-economic Analysis and Life Cycle Assessment of Producing High-Value Chemicals and Fuels from Waste Plastic via Conventional Pyrolysis and Thermal Oxo-degradation

被引:6
|
作者
Olafasakin, Olumide [1 ]
Ma, Jiaze [2 ]
Zavala, Victor [2 ]
Brown, Robert C. [1 ,3 ]
Huber, George W. [2 ]
Mba-Wright, Mark [1 ,3 ]
机构
[1] Iowa State Univ, Dept Mech Engn, Ames, IA 50011 USA
[2] Univ Wisconsin, Dept Chem & Biol Engn, Madison, WI 53706 USA
[3] Iowa State Univ, Bioecon Inst, Ames, IA 50011 USA
关键词
SYSTEM ANALYSES; SIMULATION; DESIGN; OIL;
D O I
10.1021/acs.energyfuels.3c02321
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
The rapid rise in global plastic production in recent decades has resulted in the massive generation of plastic waste. Over 75% of the plastic waste generated in the United States was sent to landfills, with a meager 8.7% recycled. Plastics are valuable feedstocks for platform chemicals and fuels. Chemical upcycling of waste high-density polyethylene (HDPE) is gaining more attention as a potentially feasible and environmentally friendly plastic waste management technology. Conventional pyrolysis (CPY) and thermal oxo-degradation (TOD) are two chemical upcycling technologies actively researched for decomposing waste HDPE into valuable chemicals and fuels. However, there are few studies on the techno-economic analysis (TEA) and life cycle assessment (LCA) of these technologies for converting waste HDPE to valuable products. This study conducts a comparative TEA and LCA study of the thermochemical decomposition of waste HDPE to produce gaseous (ethylene and propylene) and liquid (naphtha, diesel, and wax) products by CPY and TOD. The study elucidates and compares the impact of hydrocracking longer chain hydrocarbons to produce more valuable products on the TEA and LCA. The TEA showed that the fixed capital investment could range from $32.5 million for TOD without hydrocracking to $244 million for CPY with hydrocracking scenarios. Annual revenues range from $28.1 million to $71.5 million in favor of scenarios with hydrocracking. However, the net present value ranges from $1.4 million to $265.8 million in favor of scenarios without hydrocracking. Sensitivity analysis showed that fixed capital cost, facility capacity, and product prices have the biggest impact on the process economics of the facilities, while utilities and waste transportation to refineries have the biggest impact on environmental impacts. The LCA showed that primary products from scenarios without hydrocracking can be more environmentally friendly than virgin products from petroleum processes. However, TOD and CPY with hydrocracking primary products have more emissions than those of virgin products.
引用
收藏
页码:15832 / 15842
页数:11
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