Method for removing carbon dioxide, and also gas turbine installation with carbon dioxide removal

Patent metadata

Field	Value
Publication number	US-9366180-B2
Application number	US-201113825395-A
Country	US
Kind code	B2
Filing date	Sep 27, 2011
Priority date	Sep 28, 2010
Publication date	Jun 14, 2016
Grant date	Jun 14, 2016

Abstract

A method for capturing carbon dioxide is provided. In a first absorption process, carbon dioxide is absorbed by contacting a supplied carbon dioxide-containing natural gas with a first substream of a solvent. In this process a carbon dioxide-depleted natural gas and carbon dioxide-enriched solvent are formed. Then in a combustion process, the carbon dioxide-depleted natural gas is burnt, with a carbon dioxide-containing exhaust gas being formed. Then, in a second absorption process, carbon dioxide is absorbed by contacting the carbon dioxide-containing exhaust gas with a second substream of the solvent. In this process an exhaust gas freed from carbon dioxide and carbon dioxide-enriched solvent are formed. Then, in a desorption process, the first substream and the second substream of the carbon dioxide-enriched solvent are combined and carbon dioxide is desorbed by supplying heating energy, with carbon dioxide-depleted solvent being formed.

First claim

The invention claimed is:

1. A method for capturing carbon dioxide, comprising:
absorbing carbon dioxide in a first absorption process by bringing a supplied carbon dioxide-containing natural gas into contact with a first sub-stream of a solvent, a carbon dioxide-depleted natural gas and a first carbon dioxide-enriched solvent being formed;
combusting the carbon dioxide-depleted natural gas in a combustion process of a gas turbine a carbon dioxide-containing flue gas being formed; and
bringing the carbon dioxide-containing flue gas into contact with a second sub-stream of the solvent in a second absorption process, a flue gas purified of carbon dioxide and a second carbon dioxide-enriched solvent being formed;
bringing together the first and the second carbon dioxide-enriched solvent in a desorption process and carbon dioxide is desorbed through the input of thermal energy, a carbon dioxide-depleted solvent being formed,
wherein the first absorption process is carried out at a first pressure, and the first pressure corresponding to the pressure of the supplied carbon dioxide-containing natural gas, and the first pressure set higher than a second pressure set in the second absorption process.

2. The method as claimed in claim 1 , wherein the thermal energy for the desorption process is extracted from the carbon dioxide-containing flue gas.

3. The method as claimed in claim 1 , wherein the method is used in a gas turbine power plant with a gas turbine including a downstream carbon dioxide capture device and a first absorber arranged upstream of the gas turbine.

4. A gas turbine plant, comprising:
a gas turbine, which is connected on a fuel side to a fuel gas line, comprising a flue gas duct connected to a downstream carbon dioxide capture device, the carbon dioxide capture device comprising a second absorber and a desorber; and
a first absorber connected to the fuel gas line and comprising an input for a first carbon dioxide-depleted solvent, the first absorber further connected to the desorber via an absorbent line to deliver a first carbon dioxide-enriched solvent thereto;
wherein the first absorber is a high pressure absorber, which is designed for the pressure of the fuel gas line;
wherein the second absorber is a low pressure absorber, which is designed for essentially atmospheric pressure;
wherein the second absorber is further connected to the desorber to deliver a second carbon dioxide-enriched solvent thereto;
wherein the second absorber comprises an input for a second carbon dioxide-depleted solvent;
wherein the desorber is configured to remove an amount of carbon dioxide from the first and second carbon dioxide-enriched solvents, and
wherein the desorber is connected to the input of the first and second absorbers and is configured to provide the first and second carbon dioxide-depleted solvent to the first and second absorbers, respectively.

5. The gas turbine plant as claimed in claim 4 , wherein the desorber comprises a reboiler, and wherein a heat exchanger is connected into the flue gas duct, and wherein the heat exchanger is connected to the reboiler via a line, such that heat from the flue gas duct is transferred into the desorber.

6. The gas turbine plant as claimed in claim 4 , wherein the fuel gas line is a natural gas line.

7. A gas and steam turbine plant, comprising:
a gas turbine plant as claimed in claim 4 ; a steam turbine driven by a boiler, wherein the boiler is arranged downstream of the gas turbine on a flue gas side.

Assignees

• Birley Roland
• Brunhuber Christian
• Kremer Hermann
• Zimmermann Gerhard
• Siemens Ag

Inventors

• Birley Roland
• Brunhuber Christian
• Kremer Hermann
• Zimmermann Gerhard

Classifications

• B01D53/343

  Heat recovery · CPC title

• B01D2256/22

  Carbon dioxide · CPC title

• C10L3/104

  Carbon dioxide · CPC title

• Y02E20/16

  Combined cycle power plant [CCPP], or combined cycle gas turbine [CCGT] · CPC title

• B01D2252/20494

  Amino acids, their salts or derivatives · CPC title