Modeling and optimization of polygeneration system with coke-oven gas and coal gasified gas by Aspen Plus(Ⅰ)Establishment and verification of simulation process
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Modeling and optimization of polygeneration system with coke-oven gas and coal gasified gas by Aspen Plus(Ⅰ)Establishment and verification of simulation process
CIESC JournalIssue 4, Pages: 969-978(2010)
作者机构:
太原理工大学煤科学与技术教育部和山西省重点实验室,山西,太原,030024
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Online First:05 April 2010,
Published:05 April 2010
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ZHENG Anqing, FENG Jie, GE Lingjuan, et al. Modeling and optimization of polygeneration system with coke-oven gas and coal gasified gas by Aspen Plus(Ⅰ)Establishment and verification of simulation process[J]. CIESC Journal, 2010, (4): 969-978.
DOI:
ZHENG Anqing, FENG Jie, GE Lingjuan, et al. Modeling and optimization of polygeneration system with coke-oven gas and coal gasified gas by Aspen Plus(Ⅰ)Establishment and verification of simulation process[J]. CIESC Journal, 2010, (4): 969-978.DOI:
Modeling and optimization of polygeneration system with coke-oven gas and coal gasified gas by Aspen Plus(Ⅰ)Establishment and verification of simulation process
With the shortage of petroleum,liquid fuel techniques are needed to reconstruct a reliable energy framework.To solve the problem with the greenhouse gases in utilization of fossil fuel,coal based polygeneration is now becoming one of the choices.The application of coal-based polygeneration depends on the conversion of raw material to liquid fuel and decrease in the waste gas to the environment.In this study,process simulation software Aspen Plus was used to setup the module of the polygeneration system based on its mass and energy balances.Coke-oven gas and coal gasified gas were input into the system as the feeding materials,in which methane mainly from the coke-oven gas and CO2 from the coal gasified gas reacted to adjust the ratio H/C in the syngas.The main components of the greenhouse gases (CO2 and CH4) were reduced due to the CH4/CO2 reforming.The simulation includes five units,which are the unit of air separation,gas clean-up unit,reforming,production of chemical products,and combined turbine cycle.The processing units with the chemical reactions were included in the program through the dynamic and thermodynamic subroutines.Dimethyl ether (DME) and electric power are the main products from the simulated polygeneration system.The equivalent electric power efficiency (η1) and total heating efficiency (η2) were calculated.The results showed that η1,which refers to the energy quality,is more appropriate for evaluating the coal-based polygeneration system.
Modeling and optimization of polygeneration system with coke-oven gas and coal gasified gas by Aspen Plus(Ⅱ)Determination of optimal operating parameters
Catalytic performance of CuZnAl slurry catalyst prepared by complete liquid phase technology for direct synthesis DME from syngas
Complete liquid phase preparation and characterization of CuZnAlSi catalysts for DME synthesis in slurry reactor
Effect of number of stages of mixed refrigerant cycle on refrigeration performance
Conversion of dimethyl ether with DBD and RCD plasma