System and method for separating carbon dioxide from natural gas
A system and method for separating CO 2 from natural gas, which ensure that no clogging or deterioration occurs in a gas separation membrane even after the gas separation membrane is used to remove carbon dioxide from the natural gas under conditions in which the natural gas is pressurized. First, an H 2 S remover removes hydrogen sulfide from raw natural gas. Then, a compressor pressurizes the natural gas from which H 2 S has been removed. After that, a cooler cools the pressurized natural gas so as to condense components that are a part of the natural gas. A gas/liquid separator removes the condensed components, and a CO 2 separator, including a separation membrane for separating CO 2 removes CO 2 from the natural gas from which the condensed components have been removed. An expander, which shares a drive shaft with the compressor, expands the natural gas from which CO 2 has been removed and recovers energy therefrom.
1. A system for separating carbon dioxide from natural gas containing carbon dioxide and hydrogen sulfide, comprising:
a hydrogen sulfide remover for removing hydrogen sulfide from the natural gas;
a compressor for pressurizing the natural gas from which hydrogen sulfide has been removed by the hydrogen sulfide remover;
a cooler for cooling the natural gas that has been pressurized by the compressor so as to condense a component that is a part of the natural gas;
a gas/liquid separator for removing the condensed component from the natural gas that has been cooled by the cooler;
a carbon dioxide separator including a separation membrane for separating carbon dioxide from the natural gas from which the condensed component has been removed by the gas/liquid separator; and
an expander for expanding the natural gas from which carbon dioxide has been separated by the carbon dioxide separator and recovering energy from the natural gas.
2. The system according to claim 1 , wherein the cooler is a heat exchanger for exchanging heat between the natural gas that has been pressurized by the compressor and the natural gas that has been expanded by the expander.
3. The system according to claim 1 , further comprising:
a second compressor for pressurizing carbon dioxide-containing gas that has been separated by the carbon dioxide separator;
a second heat exchanger for cooling and liquefying the carbon dioxide-containing gas that has been pressurized by the second compressor;
a second gas/liquid separator for separating off-gas from the liquefied gas; and
a line for supplying the natural gas that has been expanded by the expander as cold energy source to the second heat exchanger.
4. The system according to claim 1 , further comprising:
a third heat exchanger for cooling the natural gas from which carbon dioxide has been separated by the carbon dioxide separator so as to liquefy a component that is a part of the natural gas;
a third gas/liquid separator for separating the liquefied component from the natural gas that has been cooled by the third cooler;
a line for supplying the natural gas from which the liquefied component has been separated by the third gas/liquid separator to the expander; and
a line for supplying the natural gas that has been expanded by the expander as cold energy source to the third heat exchanger.