Main Purification Operations

  • Mar Pérez-Fortes
  • Aarón D. Bojarski
Part of the Green Energy and Technology book series (GREEN)


Syngas final usage requires a previous step of cleaning and conditioning to meet with the requirements of its final use which might range from chemicals and fuels production to power and/or heat. This chapter deals with the description and the modelling of the required syngas treatment units before electricity production or before hydrogen generation, specifically in an IGCC power plant. In the case of electricity generation application, the pursued objective is to avoid as much as possible nitrogen and sulphur oxide emissions to the atmosphere. In a first step, the gas is cleaned from solids. Secondly the gas before its combustion goes through an acid and basic species removal train of units. In the case of hydrogen generation, besides syngas cleaning from other species, the main pursued objective is to separate CO from H2. In order to accomplish the former, CO should be converted into CO2 and then separated from the main stream. Hydrogen can be further purified to be sold to the market, or used in a combined cycle, in an analogous way as the syngas. Modelling calibration and validation are shown, and the chapter finishes with a model utilisation to evaluate the behaviour of the already built up superstructure to produce hydrogen or syngas for electricity generation section, or hydrogen for other applications.


Combine Cycle Pressure Swing Adsorption Integrate Gasification Combine Cycle Pressure Swing Adsorption Process Mass Flowrate 
These keywords were added by machine and not by the authors. This process is experimental and the keywords may be updated as the learning algorithm improves.



Air separation unit


Combined cycle


Carbon capture and storage


Cold gas efficiency


Cost of energy


Dimethyl ethers of polyethylene glycol


Non-random two liquid with electrolytes formation


Equation of state


Fischer–Tropsch process


Greenhouse gases


Gas turbine


Gas to liquid fuels


High pressure


Heat recovery steam generator


Integrated gasification combined cycle


Intermediate pressure


Lower heating value


Molten carbonate fuel cells


Methyl diethyl ethanol amine


Non-random two liquid


Proton exchange membranes


Pressure swing adsorption


Solid oxide fuel cell


Steam turbine


Turbine inlet temperature


Vapor–liquid equilibrium


Water gas shift


Waste heat boiler


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Copyright information

© Springer-Verlag London Limited 2011

Authors and Affiliations

  1. 1.ETSEIBUniversitat Politècnica de CatalunyaBarcelonaSpain

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