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17 275 degrees Celsius and the second temperature is less than the steam temperature, by transferring heat indi rectly to the loaded Zeolite sorbent from the steam With asecondheattransfer,therebyproducingdesorbedCO2 andH20 fromtheloadedZeolitesorbentandproducing an unloaded Zeolite sorbent; transferring the unloaded Zeolite sorbent from the regen eration reactor to the capture reactor, and cooling the unloaded Zeolite sorbent to the ?rst temperature by transferringheatfromtheunloadedZeolitesorbent; Generating an output gas stream from the regeneration reactor, Where the output gas stream is comprised of someportionoftheCO2 atmosphereandsomeportion ofthedesorbedCO2 andH20, andcoolingtheoutputgas stream to a third temperature beloW the ?rst temperature andremovingsomeportionoftheH20 intheoutputgas stream; Splittingtheoutputgasstreamatthethirdtemperatureinto aregenerationgasstreamanda?nalCO2 stream;and 18 HeatingtheregenerationstreamWithathirdheattransfer, Where the third heat transfer is comprised of heat from the transferring heat from the shifted syngas stream and heatfromthetransferringheatfromtheunloadedZeolite sorbent,anddirectingtheregenerationgasstreamtothe regenerationreactor,suchthattheCO2 atmosphereis comprisedofCO2 fromtheregenerationstream, therebyseparatingCO2 fromaprocessgasstreamcomprised ofCO2, H20 andothergaseousconstituentsinanadsorption/ desorptioncycleusingaZeolitesorbent,Wherethedesorption cycleisconductedunderconditionsofincreasedtemperature andincreasedCO2 pressuretoproducethe?nalCO2 streamat highpressure. 20. The method of claim 19 Where the shifted syngas tem perature further exceeds 200 degrees Celsius and the second temperature further exceeds 330 degrees Celsius. US 8,128,735B1PDF Image | PROCESS FOR CO2 CAPTURE USING ZEOLITES
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