Technoeconomic Feasibility of Hydrogen Production from Waste Tires with the Control of CO2 Emissions

被引:22
作者
Al-Qadri, Ali A. [1 ]
Ahmed, Usama [1 ,6 ]
Jameel, Abdul Gani Abdul [1 ,2 ,3 ]
Zahid, Umer [1 ,4 ]
Ahmad, Nabeel [2 ]
Shahbaz, Muhammad [5 ]
Nemitallah, Medhat A. [3 ,6 ,7 ]
机构
[1] King Fahd Univ Petr & Minerals, Dept Chem Engn, Dhahran 31261, Saudi Arabia
[2] King Fahd Univ Petr & Minerals, Ctr Refining & Adv Chem, Dhahran 31261, Saudi Arabia
[3] KFUPM, SDAIA KFUPM Joint Res Ctr Artificial Intelligence, Dhahran 31261, Saudi Arabia
[4] King Fahd Univ Petr & Minerals, Interdisciplinary Res Ctr Membranes & Water Secur, Dhahran 31261, Saudi Arabia
[5] Hamad Bin Khalifa Univ, Qatar Fdn, Coll Sci & Engn, Doha 34110, Qatar
[6] King Fahd Univ Petr & Minerals, Interdisciplinary Res Ctr Hydrogen & Energy Storag, Dhahran 31261, Saudi Arabia
[7] KA CARE Energy Res & Innovat Ctr Dhahran, Dhahran 31261, Saudi Arabia
关键词
BUBBLING FLUIDIZED-BED; STEAM GASIFICATION; BIOMASS GASIFICATION; PLASTIC WASTE; PYROLYSIS; SYNGAS; TEMPERATURE; CAPTURE; POLYETHYLENE; RECOVERY;
D O I
10.1021/acsomega.2c06036
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
The worldwide demand for energy is increasing significantly, and the landfill disposal of waste tires and their stockpiles contributes to huge environmental impacts. Thermochemical recycling of waste tires to produce energy and fuels is an attractive option for reducing waste with the added benefit of meeting energy needs. Hydrogen is a clean fuel that could be produced via the gasification of waste tires followed by syngas processing. In this study, two process models were developed to evaluate the hydrogen production potential from waste tires. Case 1 involves three main processes: the steam gasification of waste tires, water gas shift, and acid gas removal to produce hydrogen. On the other hand, case 2 represents the integration of the waste tire gasification system with the natural gas reforming unit, where the energy from the gasifier-derived syngas can provide sufficient heat to the steam methane reforming (SMR) unit. Both models were also analyzed in terms of syngas compositions, H2 production rate, H2 purity, overall process efficiency, CO2 emissions, and H2 production cost. The results revealed that case 2 produced syngas with a 55% higher heating value, 28% higher H2 production, 7% higher H2 purity, and 26% lower CO2 emissions as compared to case 1. The results showed that case 2 offers 10.4% higher process efficiency and 28.5% lower H2 production costs as compared to case 1. Additionally, the second case has 26% lower CO2-specific emissions than the first, which significantly enhances the process performance in terms of environmental aspects. Overall, the case 2 design has been found to be more efficient and cost-effective compared to the base case design.
引用
收藏
页码:48075 / 48086
页数:12
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