Process development of coke oven gas to methanol integrated with CO2 recycle for satisfactory techno-economic performance

被引:79
|
作者
Yi, Qun [1 ,2 ]
Gong, Min-Hui [1 ,2 ]
Huang, Yi [1 ,2 ]
Feng, Jie [1 ,2 ]
Hao, Yan-Hong [3 ]
Zhang, Ji-Long [4 ]
Li, Wen-Ying [1 ,2 ]
机构
[1] Taiyuan Univ Technol, Key Lab Coal Sci & Technol, Minist Educ & Shanxi Prov, Taiyuan 030024, Peoples R China
[2] State Key Lab Coal Sci & Technol Jointly Construc, Training Base, Taiyuan 030024, Peoples R China
[3] Shanxi Univ, Dept Environm Engn, Taiyuan 030013, Peoples R China
[4] Taiyuan Univ Technol, Coll Min Technol, Inst Mineral Resources Utilizat, Taiyuan 030024, Peoples R China
基金
中国国家自然科学基金;
关键词
Coking; Coke oven gas; CO2; recycle; System integration; Methanol; HIGH-ENERGY EFFICIENCY; TO-OLEFINS PROCESS; NATURAL-GAS; POLYGENERATION SYSTEM; EXERGY ANALYSIS; THERMOECONOMIC ANALYSIS; THERMODYNAMIC ANALYSIS; PROCESS SIMULATION; CONCEPTUAL DESIGN; ASSISTED COAL;
D O I
10.1016/j.energy.2016.06.111
中图分类号
O414.1 [热力学];
学科分类号
摘要
A novel process designed for producing methanol from coke oven gas (COG) integrated with CO2 recycle is proposed. In the new system, oxygen replacing air is blown to combustor for assisting combustion of COG and unreacted syngas from methanol synthesis process. The combustion process provides to the heat required in the coking process. The rest COG reacts with the recycled CO2 separated from the exhaust gas to produce syngas for methanol synthesis. The unreacted syngas from methanol synthesis process with low grade energy level is recycled to the combustor. In the whole methanol production process, there is no additional process with respect to supplementary carbon, and the carbon resource only comes from the internal CO2 recycle in the plant. With the aid of techno-economic analysis, the new system presents the energy or exergy saving by 5-10%, the CO2 emission reduction by about 70% and the internal rate of return increase by 5-8%, respectively, in comparison with the traditional COG to methanol process. (C) 2016 Elsevier Ltd. All rights reserved.
引用
收藏
页码:618 / 628
页数:11
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