Process and apparatus for liquefaction of CO

1 . A process for the liquefaction and subcooling of a stream rich in CO 2 containing at least 95 mol % of carbon dioxide comprising the following steps:

i. liquefying the stream rich in CO 2 at a subcritical pressure greater than 48 bars abs, through an indirect heat exchange in a heat exchanger having a hot end and a cold end with an at least partially liquid stream of a refrigerant different from CO 2 at a first pressure greater than 4 bara in which the liquid stream of refrigerant different from CO 2 vaporizes to form a gaseous stream of refrigerant different from CO 2 at the first pressure and the CO 2 -rich stream liquefies to form a CO 2 -rich liquid stream at a subcritical pressure,

ii. subcooling the CO 2 -rich liquid stream or a fluid formed by separating the CO 2 -rich liquid stream, through indirect heat exchange in the heat exchanger with at least three other liquid streams rich in CO 2 which each vaporize at a different pressure,

iii. compressing the gaseous stream of refrigerant different from CO 2 or a stream formed by separating said gaseous stream of refrigerant different from carbon dioxide, the compression taking place in a compressor from the first pressure to a second pressure greater than the first pressure in order to obtain a gas stream of refrigerant different from CO 2 , at the second pressure in a single compression stage, no gas flow being sent to an intermediate level of the compressor

iv. condensing the gaseous stream of refrigerant different from CO 2 at the second pressure or a stream resulting therefrom in order to obtain a liquid stream of ammonia at the second pressure

v. cooling the refrigerant liquid stream to the second pressure in the heat exchanger and

vi. expanding either the cooled liquid stream of refrigerant different from CO 2 at the second pressure or a stream formed by separating the liquid stream of refrigerant different from CO 2 up to the first pressure in order to obtain the at least partially liquid stream of refrigerant different from CO 2 up to a single pressure which is the first pressure.

2 . The method according to claim 1 in which the first pressure is greater than 5 bara.

3 . The method according to claim 1 , in which the gas stream rich in CO 2 condenses at a temperature between 5° C. and 15° C.

4 . The method according to claim 1 , wherein the refrigerant circulates in a closed loop and the inlet temperature of the refrigerant compressor is the temperature at which the refrigerant different from CO 2 leaves the hot end of the heat exchanger.

5 . The method according to claim 1 , wherein the gaseous stream of refrigerant different from CO 2 leaves the compressor and enters the hot end of the heat exchanger after having been condensed against air or water.

6 . The method according to claim 1 , wherein a part of the liquid stream rich in CO 2 at a subcritical pressure is expanded to form the at least three other liquid streams rich in CO 2 vaporizing at at least three different pressure levels.

7 . The method according to claim 1 , wherein at least one stream of liquid CO 2 vaporizing at at least one pressure level enters the cold end of the heat exchanger.

8 . The method according to claim 1 , wherein the expanded liquid refrigerant is at an intermediate temperature of the heat exchanger.

9 . The method according to claim 1 , wherein the expanded liquid refrigerant is sent to heat up in the heat exchanger at an intermediate point between the cold end and the hot end of the heat exchanger.

10 . The method according to claim 1 , wherein the refrigerant compressor comprises only a single compression section.

11 . The method according to claim 1 , wherein the inlet pressure of the refrigerant compressor is greater than 4 bara.

12 . The method according to claim 1 , wherein the refrigerant remains entirely in liquid form after the expansion step vi).

13 . An apparatus for liquefying and subcooling a stream rich in CO 2 containing at least 95 mol % of carbon dioxide comprising a heat exchanger having a hot end and a cold end, a means for sending the stream rich in CO 2 at a subcritical pressure greater than 48 bar abs, liquefy through indirect heat exchange in the heat exchanger with an at least partially liquid stream of a refrigerant different from CO 2 at a first pressure greater than 4 bara in which the liquid stream of refrigerant different from CO 2 , vaporizes to form a gaseous stream of refrigerant different from CO 2 at the first pressure and the stream rich in CO 2 liquefies to form a CO 2 -rich liquid stream at subcritical pressure, a means for subcooling the CO 2 -rich liquid stream or a fluid formed by separating the CO 2 -rich liquid stream, through an exchange of indirect heat in the heat exchanger with at least three other liquid streams rich in CO 2 which each vaporize at a different pressure, therefore at at least three different pressure levels, a compressor for compressing the gaseous stream of refrigerant different from CO 2 or a stream formed by separating this gaseous stream, the compression taking place in the compressor from the first pressure to a second pressure greater than the first pressure in order to obtaining a gas stream of refrigerant different from CO 2 at the second pressure in a single compression step, no gas flow being sent to an intermediate level of the compressor, a means for condensing the gas stream of refrigerant different from CO 2 at the second pressure or a current coming from it in order to obtain a liquid stream of ammonia at the second pressure, a means for sending the liquid stream of condensed refrigerant at the second pressure to cool in the exchanger heat and a means for expanding either the cooled liquid stream of refrigerant different from CO 2 to the second pressure or a stream formed by separating the liquid stream of refrigerant different from CO 2 to the first pressure in order to obtain the at least partially liquid stream of refrigerant different from CO 2 up to a single pressure which is the first pressure.