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Simulation Research Of CO2?1?/Low Rank Coal Slurry Gasification System Based On Aspen Plus

Posted on:2017-07-16Degree:MasterType:Thesis
Country:ChinaCandidate:C J DengFull Text:PDF
GTID:2311330482987029Subject:Mechanical engineering
Abstract/Summary:PDF Full Text Request
Under the background of demand to steady energy supply and low carbon emission in China,the technology of coal water slurry?CWS?gasification has been considered as an effective clean coal technology.It has been widely studied and used recently.The reserve of LRC?low rank coal?reaches more than 50 percent of the gross reserve in China.It is suitable to be converted into gas by CWS gasification process.However,the solid concentration of CWS and gasification efficiency are very low for LRC.Compared to CWS,Liquid CO2?CO2?1??slurry has lots of advantages,such as low latent heat of vaporization,ability to improve the dispersion of the coal in the gasifier,comparatively high concentration of coal slurry and less CO2 emissions.Therefore,CO2?1?slurry is suitable for LRC gasification.This work focus on the simulation of LRC-CO2?1?slurry gasification in Aspen Plus.This would provide a theoretical basis for the applications of LRC gasification.Firstly,an Aspen Plus model for simulation of the gasification of LRC-CO2?1?slurry was developed.The laboratory experimental results were used to validate this model.Then,the influence of different parameters on gasification reaction were mainly performed,such as coal characteristics,the ratio of oxygen to coal,concentration of CO2?1?slurry,pressure and different ratio of H2 O to CO2,and so on.Finally,comparion analysis between LRC-CO2?1?slurry and CWS for an IGCC system were further studied.It can be seen from the results that temperature in the gasifier increased with rising of O2/coal.O2/coal also significantly influenced the composition of syngas.The concentration of CO and H2 in syngas rose with O2/coal and then decreased when O2/coal exceeded 0.72.CO and H2 content in syngas increased at higher concentration of LRC-CO2?1?slurry,the temperature in gasifier also increased accordingly.The concentration of the slurry should be set at about 60%.When O2/coal and slurry concentration were all taken into consideration,the best operating conditions appeared at 0.74 of O2/coal with 60% slurry concentration.Pressure in the gasifier didn't significantly affect the gasification procedure.When H2 O was used to replace part of the CO2,higher H2O/CO2 led to more H2 content in syngas,while the percentage of CO went to opposite tendency more rapidly.Wide range of H2/CO could be expected,which offered a flexible adaptivity according to the different demands.Besides,the emission of CO2 also reduced.Simulation research of the IGCC system in Aspen Plus was conducted.It was found that LRCCO2?1?slurry could greatly enhance the usage of the LRC.The IGCC system reached to a higher carbon conversion rate and net effiency when using LRC-CO2?1?slurry.Furthermore,the amount of water consumption,CO2 emission and energy consumption decreased.The results show that great economic and environmental benefits will be accomplished by the introduction of LRC-CO2?1?slurry in IGCC system.
Keywords/Search Tags:Low Rank Coal, Coal Gasification, Liquid CO2 coal slurry, Simulation Research, Aspen Plus
PDF Full Text Request
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