Patent ID: 8887510

Claim:
A method for power production by combustion of carbonaceous fuels and CO 2 capture, where the carbonaceous fuel is combusted in a combustion chamber under pressure in presence of gas containing oxygen, where the combustion gas is cooled in the combustion chamber by generation of steam inside heat pipes provided in the combustion chamber, where the exhaust gas is withdrawn from the combustion chamber through an exhaust gas pipe via heat exchanger(s) and exhaust gas treatment units, and a direct contact cooler connected to a water recycle pipe for recirculation of water collected at the bottom of the direct contact cooler and reintroduction of the water at the top of the cooler, in which cooler the partly cooled exhaust gas is further cooled and humidified by counter-current flow to water, where the exhaust gas is withdrawn from the direct contact cooler through a cleaned exhaust pipe and is introduced into a CO 2 absorber, into which absorber lean absorbent is introduced above an upper contact zone in the absorber, to cause the exhaust gas to flow counter-current to a liquid CO 2 absorbent to give a rich absorbent that is collected at the bottom of the CO 2 absorber and is withdrawn therefrom in a rich absorbent pipe, and a CO 2 lean exhaust gas that is withdrawn from the top of the absorber through a lean exhaust pipe connected to the absorber, where the lean exhaust gas is washed in a washing section, heated in a heat exchanger and expanded over a turbine for generation of electrical power before being released into the atmosphere; where the rich absorbent pipe is connected to introduce the rich absorbent into stripping column for regeneration of the absorbent to give a lean absorbent that is withdrawn through a lean absorbent recycle line in which the lean absorbent is pumped back to into the absorber, and a CO 2 stream that is further treated to give clean CO 2 ; wherein the CO 2 stream is cooled against cooling fluid flowing through the direct contact cooler direct contact cooler provided at the top of the stripping column; and wherein water is collected at a collector plate provided below the direct contact cooler, and where a water recycle line is arranged to withdraw the collected water, wherein the circulating direct contact cooler cooling water in the recirculation pipe is cooled in a heat exchanger provided in the recirculation pipe, where cooling water is delivered and withdrawn, respectively, through water recycle pipes connected to the heat exchanger, and where the water withdrawn from the heat exchanger through recycle line is flashed over a flash valve and a flash tank, where water from the flash tank is withdrawn through a line to recycle the water as washing liquid in the stripping column direct contact cooler; and wherein the vapour in the stripping tank is introduced as additional stripping vapour in the stripping column through a vapour line connected to the flash tank.