By Malcolm Wilson, E.S. Rubin, D.W. Keith, C.F. Gilboy, T. Morris, K. Thambimuthu, John Gale

Following the profitable booklet of the court cases of sixth eco-friendly apartment gasoline keep watch over know-how convention (GHGT-6), Elsevier is proud to submit the complaints from the seventh convention, held in Vancouver in September 2004.

The Greenhouse fuel regulate applied sciences convention sequence has tested itself because the most appropriate convention bringing jointly the foreign power group, offering a discussion board for the dialogue of the newest advances within the box of greenhouse gasoline keep an eye on applied sciences.

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Extra resources for Greenhouse Gas Control Technologies 7. Proceedings of the 7th International Conference on Greenhouse Gas Control Technologies 5– September 2004, Vancouver, Canada

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Chem. Lett. 9, 777-778 Bishnoi, S. and G. T. Rochelle, 2000. Absorption of Carbon Dioxide into Aqueous Piperazine: Reaction Kinetics, Mass Transfer and Solubility. Chem. Eng. Sci. 55, 5531-5543 Austgen, D. ,1989. A Model of Vapor-Liquid Equilibria for Acid Gas-Alkanolamine-Water Systems. D. dissertation, The University of Texas at Austin. Wilson, G. , D. M. VonNiederhausern, and N. F. Giles, 2002. Critical Point and Vapor Pressure Measurement for Nine Compounds by a Low Residence Time Flow Method.

There needs to be accurate knowledge of what these results are, and realism in their interpretation for a fair score to be derived. Although weighting factors in the program are locked if there is a need to change factors, for example to describe a different future scenario, an alternative version of the program could be made or a set of several different selectable scenarios could be built in. R E S U L T S OF E V A L U A T I O N S - THE S E A R C H FOR A B E T T E R P R O C E S S Presentation of Results For each evaluation a separate Excel file has been prepared.

1 )01 ; , ..... 01 i i | i = i=l I 0. 9 M AEEA solutions New Method for Comparison of Absorbent Performance As noted above the difference between AEEA and MEA is not very clear, and a better way of comparing the absorbents is needed. A comparison AEEA and MEA for CO2 recovery can be made by using a combination of the VLE data in Figure 6 together with the rate data from Figure 4. If, as a first order estimate, it is assumed that equilibrium is attained in both the absorption and stripping steps, the net cyclic capacity (Q) can then be defined as: oEm°'c°2 so _ (2) tool 5O ....

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