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Sökning: id:"swepub:oai:DiVA.org:mdh-32406" > Impacts of thermo-p...

Impacts of thermo-physical properties of gas and liquid phases on design of absorber for CO2 capture using monoethanolamine

Nookuea, Worrada (författare)
Mälardalens högskola,Framtidens energi
Tan, Yuting (författare)
KTH,Skolan för kemivetenskap (CHE),School of Chemical Science and Engineering, Royal Institute of Technology, Stockholm, Sweden
Li, Hailong (författare)
Mälardalens högskola,Framtidens energi
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Thorin, Eva (författare)
Mälardalens högskola,Framtidens energi
Yan, Jinyue (författare)
KTH,Mälardalens högskola,Framtidens energi,School of Chemical Science and Engineering, Royal Institute of Technology, Stockholm, Sweden,Energiprocesser,Mälardalen University, Sweden
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 (creator_code:org_t)
Elsevier BV, 2016
2016
Engelska.
Ingår i: International Journal of Greenhouse Gas Control. - : Elsevier BV. - 1750-5836 .- 1878-0148. ; 52, s. 190-200
  • Tidskriftsartikel (refereegranskat)
Abstract Ämnesord
Stäng  
  • Absorption of CO2 with aqueous amines in post-combustion capture is characterized as a heat and mass transfer processes with chemical reaction, which is sensitively affected by the thermo-physical properties of fluids. In order to optimize the design of the absorber of CO2 capture process, in this paper, the impacts of thermo-physical properties on the column design were investigated. Furthermore, the property impacts on the capital cost of the absorber unit were also identified and analyzed. Results show that the gas phase density has the most significant effect on the column diameter. Underestimation of the gas phase density of 10% may result in an increase of about 6% of the column diameter. For the packing height, the liquid phase density has the most significant effect. 10% underestimation of the liquid phase density may result in an increase of 8% of the packing height. Moreover, the effect from the liquid phase viscosity is also significant. For the annual capital cost, the liquid phase density also shows the most significant effect. Underestimation of the liquid phase density of 10% leads to the cost overestimation of $1.4 million for the absorption column for a 400 MW coal-fired power plant. Therefore, the development of the flue gas density model and liquid phase density and viscosity models of the aqueous amine solution with CO2 loading should be prioritized.

Ämnesord

TEKNIK OCH TEKNOLOGIER  -- Maskinteknik -- Energiteknik (hsv//swe)
ENGINEERING AND TECHNOLOGY  -- Mechanical Engineering -- Energy Engineering (hsv//eng)

Nyckelord

Chemical absorption
Density
Packing height
Post-combustion capture
Property impact
Viscosity
Carbon dioxide
Coal
Coal combustion
Combustion
Costs
Density (specific gravity)
Fossil fuel power plants
Gases
Liquids
Mass transfer
Physical properties
Absorption columns
Coal-fired power plant
Heat and mass transfer process
Liquid phase viscosity
Post-combustion captures
Thermo-physical property
Density of gases

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