Densities of the carbon dioxide + hydrogen, a system of relevance to carbon capture and storage

Abstract The densities of the carbon dioxide (CO2) and hydrogen (H2) mixtures ( x H 2 = 0.020,0.075 and 0.100 ) have been determined at six temperatures from 288.15 to 333.15 K and pressures up to 23.0 MPa using a high-pressure vibrating-tube densitometer. The experimental temperatures and pressures cover a range of sub- and supercritical conditions, providing essential information for the optimum design and operation of compressors and pipeline networks in carbon capture and storage (CCS). It was found that a concentration of H2 as low as 2% could lower the density by as much as 25% compared to pure CO2. The data were used to calculate the excess molar volumes, showing highly non-ideal mixing behaviour of the binary system of CO2 + H2. The new density data were also compared to those predicted using the GERG-2004 equation of state (Kunz, O. et al., 2007. The GERG-2004. Wide-range equation of state for natural gases and other mixtures, Dusseldorf). The deviations between the calculated and experimental data are 0.6%, 1.7% and 1.8%, respectively, for the mixtures with x H 2 = 0.020,0.075 and 0.100 . These results suggest that the GERG-2004 equation of state has the potential for accurate prediction of the volumetric property of CO2 mixtures containing H2 in the CCS processes, and further parameterisation of GERG-2004 or development of new equations of state specifically tailored for CCS mixtures is required.

[1]  P. H. van Konynenburg,et al.  Critical lines and phase equilibria in binary van der Waals mixtures , 1980, Philosophical Transactions of the Royal Society of London. Series A, Mathematical and Physical Sciences.

[2]  B. D. Abadio,et al.  (Pressure, amount-of-substance density, temperature) of {(1-x)CO2+xH2} using a direct method , 1993 .

[3]  A. Chambers,et al.  World Energy Outlook 2008 , 2008 .

[4]  H. Huemer,et al.  Investigations on the limits of uncertainty of gas density measurements with vibrating tube densimeters , 1998 .

[5]  P. L. Barrick,et al.  LIQUID-VAPOR EQUILIBRIA OF THE HYDROGEN-CARBON DIOXIDE SYSTEM. , 1968 .

[6]  B. E. Gammon,et al.  Densities of Carbon Dioxide + Nitrogen from 225 K to 450 K at Pressures up to 70 MPa , 1997 .

[7]  J Davison,et al.  An overview of technologies and costs of carbon dioxide capture in power generation , 2009 .

[8]  Manuela Artal,et al.  Experimental setup to measure critical properties of pure and binary mixtures and their densities at different pressures and temperatures: Determination of the precision and uncertainty in the results , 2008 .

[9]  W. Wagner,et al.  The GERG-2008 Wide-Range Equation of State for Natural Gases and Other Mixtures: An Expansion of GERG-2004 , 2012 .

[10]  M. Poliakoff,et al.  Method for locating the vapor-liquid critical point of multicomponent fluid mixtures using a shear mode piezoelectric sensor. , 2005, Analytical chemistry.

[11]  A. John Mallinckrodt,et al.  Data Reduction and Error Analysis for the Physical Sciences , 1993 .

[12]  Fariba Dehghani,et al.  Vapor-liquid equilibrium for binary systems of carbon dioxide + methanol, hydrogen + methanol, and hydrogen + carbon dioxide at high pressures , 2002 .

[13]  Hailong Li,et al.  PVTxy properties of CO2 mixtures relevant for CO2 capture, transport and storage: Review of available experimental data and theoretical models , 2011 .

[14]  Jinyue Yan,et al.  Impacts of equations of state (EOS) and impurities on the volume calculation of CO2 mixtures in the applications of CO2 capture and storage (CCS) processes , 2009 .

[15]  James G. Blencoe,et al.  Volumetric properties for {(1 –x)CO2+xCH4},{(1 −x)CO2+xN2}, and {(1 −x)CH4+xN2} at the preessures (19.94, 29.94, 39.94, 59.93, 79.93, and 99.93) MPa and the temperature 673.15 K , 1996 .

[16]  Jürgen Gmehling,et al.  Densities of Toluene, Carbon Dioxide, Carbonyl Sulfide, and Hydrogen Sulfide over a Wide Temperature and Pressure Range in the Sub- and Supercritical State , 2001 .

[17]  C. Y. Tsang,et al.  Phase equilibria in the H2/CO2 system at temperatures from 220 to 290 K and pressures to 172 MPa , 1981 .

[18]  W. Wagner,et al.  A New Equation of State for Carbon Dioxide Covering the Fluid Region from the Triple‐Point Temperature to 1100 K at Pressures up to 800 MPa , 1996 .

[19]  W. M. Haynes,et al.  Isochoric (p, Vm, T) measurements on CO2 and on (0.982CO2+0.018N2) from 250 to 330 K at pressures to 35 MPa , 1989 .

[20]  B. Metz IPCC special report on carbon dioxide capture and storage , 2005 .

[21]  H. Herzog,et al.  Scaling up carbon dioxide capture and storage: From megatons to gigatons , 2011 .

[22]  Hailong Li,et al.  Evaluating cubic equations of state for calculation of vapor–liquid equilibrium of CO2 and CO2-mixtures for CO2 capture and storage processes , 2009 .

[23]  Hailong Li,et al.  Impurity impacts on the purification process in oxy-fuel combustion based CO2 capture and storage system , 2009 .

[24]  Andrea Cipollina,et al.  Experimental P−T−ρ Measurements of Supercritical Mixtures of Carbon Dioxide, Carbon Monoxide, and Hydrogen and Semiquantitative Estimation of Their Solvent Power Using the Solubility Parameter Concept , 2007 .

[25]  P. R. Bevington,et al.  Data Reduction and Error Analysis for the Physical Sciences , 1969 .

[26]  H. Vos Trade and Industry , 1946 .

[27]  M. Mølnvik,et al.  Dynamis CO2 quality recommendations , 2008 .