Method and apparatus for collecting carbon dioxide from flue gas
An apparatus for collecting carbon dioxide from flue gas of a power plant. The apparatus includes an absorption tower, a sedimentation pool including slanting boards, a regeneration tower, a gas-liquid separator, a desiccator, a compressor, and a condenser. A rich solution is adapted to flow from a bottom of the absorption tower into the sedimentation pool for stratification. A gas outlet of the gas-liquid separator is in series connection with the desiccator, the compressor, the condenser, and a liquid carbon dioxide storage tank.
1. An apparatus for collecting carbon dioxide from flue gas of a power plant, the apparatus comprising: an absorption tower, a sedimentation pool comprising slanting boards, a regeneration tower, a gas-liquid separator, a desiccator, a compressor, and a condenser; a rich solution flowing from a bottom of the absorption tower into the sedimentation pool comprising the slanting boards for stratification; a gas outlet of the gas-liquid separator being in series connection with the desiccator, the compressor, the condenser, and a liquid carbon dioxide storage tank, wherein
a bottom flow outlet of the sedimentation pool comprising the slanting boards is connected to a first medium inlet of a second heat exchanger via a pipe where a rich solution pump is disposed; a supernatant overflow of the sedimentation pool comprising the slanting boards is connected to an inlet of a circulating absorption solution storage tank via a pipe; an outlet of the circulating absorption solution storage tank is connected to a spray pipe of a spray layer in the absorption tower via a pipe where an absorption solution circulating pump is disposed;
a first medium outlet of the second heat exchanger is connected to a first medium inlet of a first heat exchanger via a pipe; a first medium outlet of the first heat exchanger is connected to an inlet disposed on an upper part of the regeneration tower via a pipe; a gas outlet disposed on a top of the second heat exchanger is connected to a pipe connecting the first heat exchanger and a cooler; a gas outlet disposed on an upper part of the regeneration tower is connected to a second medium inlet of the first heat exchanger via a pipe; a second medium outlet of the first heat exchanger is connected to an inlet of the cooler via a pipe; an outlet of the cooler is connected to an inlet of the gas-liquid separator via a pipe; and
a liquid outlet disposed on a lower part of the regeneration tower is connected to a second medium inlet of the second heat exchanger via a pipe where a lean solution pump is disposed; a second medium outlet of the second heat exchanger is connected to the inlet of the circulating absorption solution storage tank via a pipe where a filter is disposed; a condensate overflow of the gas-liquid separator is connected to the inlet of the circulating absorption solution storage tank via a pipe; a solution storage tank for storing an aqueous solution of a composite absorbent is connected to the inlet of the circulating absorption solution storage tank via a pipe where a solution pump is disposed.
2. The apparatus of claim 1 , wherein
the absorption tower is a pneumatic bubbling tower; a sieve plate, a pneumatic bubbling layer, a filler layer, and a demister are respectively arranged bottom up in the absorption tower between a flue gas inlet arranged on a lower part of the absorption tower and a flue gas outlet arranged on a top of the absorption tower;
the absorption tower is further provided with a spray layer, and the spray layer is provided with between 2 and 4 spray pipes; a plurality of nozzles are disposed on each spray pipe;
the sieve plate comprises circular through-holes, and an area ratio of the circular through-holes and the sieve plate is between 30 and 40%; and
the demister comprises: an upper filter screen, a lower filter screen, and a spray unit disposed therebetween.