A novel hydrogen pressure swing adsorption system has been studied that is applied to an advanced integrated gasification combined cycle plant for cogenerating power and ultrapure hydrogen (99.99+ mol%) with CO 2 capture. In designing the H 2 PSA, it is essential to increase the recovery of ultrapure hydrogen product to its maximum since the power consumption for compressing the H 2 PSA tail gas up to the gas turbine operating pressure should be minimised to save the total auxiliary power consumption of the advanced IGCC plant. In this study, it is sought to increase the H 2 recovery by increasing the complexity of the PSA step configuration that enables a PSA cycle to have a lower feed flow to one column for adsorption and more pressure equalisation steps. As a result the H 2 recovery reaches a maximum around 93 % with a Polybed H 2 PSA system having twelve columns and the step configuration contains simultaneous adsorption at three columns and four-stage pressure equalisation.
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Luberti et al. (2013) studied this question.
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