System and method for co 2 desorption from a solvent

Abstract

A system for separating CO2 from an exhaust gas of a large engine by means of a solvent which is capable of reversibly absorbing CO2 from the exhaust gas to generate rich solvent and capable of desorbing a CO2 comprising fluid to regenerate lean solvent, wherein the system is in particular configured for use on board of a marine vessel, the system comprising an absorption container configured to receive the exhaust gas comprising CO2 from the large engine and lean solvent, wherein the lean solvent absorbs at least a part of the CO2 from the exhaust gas, thereby producing rich solvent and exhaust gas having a reduced CO2 content a desorption container configured to receive rich solvent from the absorption container, wherein the desorption container is configured to evaporate the CO2 comprising fluid from the rich solvent in a desorption process such that lean solvent is regenerated a first line connecting the absorption container to the desorption container the first line being configured to transfer rich solvent from the absorption container to the desorption container a second line connecting the desorption container to the absorption container, the second line being configured to transfer lean solvent from the desorption container back to the absorption container and a low-pressure source in a fluid connection with the desorption container configured such that a low-pressure generated by the low-pressure source enhances the evaporation of the CO2 comprising fluid from the rich solvent in the desorption container.

Description

[0001] WinGD Ltd.

[0002] W32172WO

[0003] System and method for CO2 desorption from a solvent

[0004] Technical field

[0005] The present invention is related to the field of chemical absorption carbon capture systems. Specifically, it relates to a system, and a method for CO2 desorption from a solvent capable of reversibly absorbing and desorbing CO2 from an exhaust gas of a large engine. Further, it relates to a propulsion system for a marine vessel comprising such a system. Another aspect relates to a use of a vacuum ejector for such a system.

[0006] Background

[0007] Large engines, which can be configured as two-stroke or four-stroke engines, for example, as longitudinally scavenged two-stroke large engines or two-stroke cross-head engines, are often used as drive units for ships, particularly large ships and vessels for the transport of goods, or in stationary operations such as driving large generators for generating electrical energy. The engines usually run for considerable periods in continuous operation, which places high demands on operational safety and availability. As a consequence, particularly long maintenance intervals, low wear, and economical handling of the operating materials are central criteria for the operator. Large engines typically have cylinders with an inner diameter (bore) of at least 200 mm. Nowadays, large engines with a bore of up to 980 mm or even more are used. Within the framework of this application, the term "large engine" designates an internal combustion engine with a bore of the cylinder(s) that is at least 200 mm and preferably at least 300 mm. Engine speed is preferably below 800 RPM, especially for four-stroke engines, and more preferably below 200 RPM for two-stroke engines, which indicates the designation of low-speed engines.

[0008] Large engines are classically configured as large diesel engines, which are operated with heavy fuel oil. The engine can be a diesel or a gas engine, a dual-fuel or a multi-fuel engine. Under the aspects of economic and efficient operation, compliance with exhaust-gas limit values, sustainability, reduction of CO2emissions, and the availability of resources, alternatives to heavy fuel oil are now also being sought for large engines. In this respect, both liquid fuels, i.e., fuels that are introduced into the combustion chamber in the liquid state, and gaseous fuels, i.e., fuels that are introduced into the combustion chamber in the gaseous state, are used.

[0009] Examples of liquid fuels as known alternatives to heavy fuel oil are other heavy hydrocarbons, which are particularly left over as residues from oil refining; alcohols, in particular methanol or ethanol; ammonia; gasoline; diesel; or also emulsions or suspensions such as slurries. Biological fuels, such as oil made from algae or seaweed, HVO (hydro-treated vegetable oil), and FAME (fatty acid methyl ester) based fuels are also possible. For example, it is known to use emulsions known as MSAR (Multiphase Superfine Atomized Residue) as fuel. As gaseous fuels, natural gases such as LNG (liquefied natural gas), liquefied gases such as LPG (liquefied petroleum gas), natural gas (NG), petrol gas (PG), ethane, or hydrogen are known. Further possible fuels comprise LBG (liquefied biogas), hydrogen, ammonia, and synthetic fuels from CO2(e.g., made by Power-To-Gas or Power-To-Liquid processes).

[0010] In particular, large engines are also known which can be operated with at least two or even more different fuels, whereby the engine is operated either with one fuel or with the other fuel depending on the operating situation or environment. It is also known to concurrently inject the two different fuels into the combustion chamber of the cylinder.

[0011] Large engines that can be operated with two or more different fuels are referred to as dual-fuel or multi-fuel large engines. Depending on the fuels, these engines may be operated in a liquid mode, in which a liquid fuel is introduced into the cylinder for combustion, and / or in a gas mode, in which a gas is introduced into the cylinder as fuel.

[0012] Large engines, which can be operated with at least two or even more different liquid or gaseous fuels, are often operated in different operating modes depending on the fuel currently in use. In the operating mode often referred to as diesel operation, the combustion of the fuel generally takes place according to the principle of compression ignition or self-ignition of the fuel. In the mode often referred to as Otto operation, combustion takes place by induced ignition. This induced ignition can take place, for example, by an electrical spark (e.g., with a spark plug) or by the self-ignition of a small injected amount of fuel (pilot fuel), which then causes the induced ignition of another fuel. The small amount of fuel intended for self-ignition is directly inserted into the combustion chamber or injected into a pre-chamber connected to the combustion chamber. Forced ignition can thus be achieved by use of a pre-chamber, a spark plug, and / or a pilot fuel. The process of induced ignition by self-ignition of a small amount of a liquid or another self-igniting fuel is sometimes referred to as pilot injection.

[0013] Furthermore, mixed forms using both Otto and diesel operation are also known.

[0014] In particular, in view of attempts to reduce greenhouse gas emissions, the reduction of CO2production, and sustainability goals, a reduction in the use of fossil fuels is strived for. Thus, alternatives are investigated to at least reduce or even completely avoid the use of fossil fuels in large engines. Even if this is still a long way off, a partial replacement of fossil fuels by renewable fuels is considered a significant success. One alternative to fossil fuel is, for example, methanol or ammonia. However, such renewable fuels can cause corrosion problems in the fuel distribution and injection system, in particular during standstill of the engine, when the stagnant methanol can corrosively attack the pipes or other components of the fuel injection system. Furthermore, there is the risk that these fuels escape from the engine, e.g., as vapor, into the space which is accessible to engine maintenance or operating personnel. This constitutes a health hazard requiring comprehensive mitigation measures.

[0015] The escaping of gaseous fuel into the atmosphere are usually referred to as fuel slip or fugitive emissions. When methanol or ammonia is used as a fuel in a large engine, most of the methanol or ammonia is consumed in the combustion process. However, some of the fuel remains unburned and may escape into the atmosphere, e.g., by passing through the exhaust gas system of the large engine (fuel slip). All upstream losses are summarized as fugitive emissions.. Methanol or ammonia is hazardous for the environment as well as for humans and animals. Therefore, great efforts are made to reduce the fuel slip occurring in large engines, such as those used for ship propulsion.

[0016] Use of fossil fuels and other alternative fuels in large engines contribute greatly to greenhouse gases and to the existing climate crisis. In attempts to reduce greenhouse gas emissions, reducing CO2 emissions in exhaust gases of power plants and industries or other sources in the environment are of utmost importance. Absorption of CO2 using a suitable solvent is one of the most prevalent and popular methods of carbon capture practised today. Physical or chemical (or a combination of both) solvents for absorption of CO2 can be adapted according to the requirements, where both the methods have advantages and disadvantages over the other. Chemical method of carbon capture is more widely practiced where the thermodynamic conditions do not favour a physical absorption process, wherein the chemical solvent has higher CO2 absorption and desorption potential.

[0017] On-board chemical absorption carbon capture requires CO2 desorption to regenerate the solvent in order to enable a cyclic, sustainable operation. This usually involves high energy demands. The process can be briefly described as follows: a suitable chemical solvent is introduced into an absorption unit, where it only reacts and dissolves CO2 from an exhaust gas, to form a temporary weak chemical structure while not reacting with any other gases. This (CO2) rich solvent can be regenerated by heating it to release the trapped CO2 molecule and thereby regenerating the (CO2) lean solvent that can then be used again for CO2 absorption. Hence, the rich solvent from the absorption unit is then transferred to a desorption unit where it is stripped off the absorbed CO2 and the regenerated solvent is recycled and reused for the absorption process in the absorption unit. Although absorption of CO2 raises the temperature of this solvent, it needs to be further heated to a temperature of ~12O-13O°C. An external heating source or a reboiler is used to heat the solvent in the desorption unit. The regenerated (CO2 stripped) lean solvent is then recirculated and reused in the absorption unit. Whereas the desorbed CO2 is cooled and compressed to liquify and are stored in suitable containers.

[0018] The desorption unit may utilize the steam generated by exhaust gas to heat up the rich solvent. In large engines, the steam quality (temperatures and pressures) from the exhaust gas is not always optimum for raising the temperature of the solvent up to -120-130 °C. While such temperatures might be achieved when the engine is working at its full load capacity, at partial engine loads, the waste heat is insufficient in quantity and / or quality to raise the temperature of the solvent to enable a sufficient CO2 desorption process. Thus, other, e.g. fuel intensive (combustion) form for generating required desorption heat is usually used.

[0019] Besides, heating the solvent to higher temperatures may lead to corrosion and quality degradation of the solvent, thereby affecting its CO2-absorption capabilities. Therefore, it is important to find improved methods for desorption of CO2 from the solvent.

[0020] Disclosure of the invention

[0021] On-board chemical absorption carbon capture is an energy intense yet very crucial process to curb CO2 concentration in the atmosphere. Presently known methods of on-board chemical absorption carbon capture from the exhaust gas of large engines involve a number of steps leading up to absorption and desorption of CO2 from a solvent. The known methods involve several challenges which will be addressed herein. It is an objective of the present invention to at least in part overcome the drawbacks of the prior art solutions and in particular to provide a system, a method, and a propulsion system for a marine vessel, which enable a more efficient and / or widely applicable CO2 capturing process.

[0022] According to a first aspect of the invention, this objective is achieved by a system for separating CO2 from an exhaust gas of a large engine by means of a solvent which is capable of absorbing CO2 from the exhaust gas to generate rich solvent and capable of desorbing a CO2 comprising fluid to regenerate lean solvent, wherein the system is in particular configured for use on board of a marine vessel, the system comprising an absorption container configured to receive the exhaust gas comprising CO2 from the large engine and a non-CO2 comprising solvent or lean solvent. The lean solvent absorbs at least a part of the CO2 from the exhaust gas, thereby producing CO2 comprising solvent or rich solvent and exhaust gas having a reduced CO2 content. The CO2 comprising solvent is called “rich solvent” herein to denote that the solvent is “loaded” with CO2 from the exhaust gas. The non-CO2 comprising solvent is called “lean solvent” herein to denote that the solvent is “available” for loading with CO2 from the exhaust gas. It should be noted that the term “non-CO2 comprising solvent” does not necessarily mean that no CO2 is present at all, but only that the solvent has capacity to be loaded with CO2 from the exhaust gas. Further, the system comprises a desorption container which is configured to receive the rich solvent from the absorption container. The desorption container is configured to evaporate a CO2 comprising fluid from the rich solvent in the container in a desorption process such that lean solvent is regenerated. The lean solvent can be reused in the system.

[0023] Furthermore, the absorption container is connected to the desorption container by a first line configured to transfer the rich solvent from the absorption container to the desorption container. Furthermore, a second line connecting the desorption container to the absorption container is provided, wherein the second line is configured to transfer lean solvent from the desorption container back to the absorption container.

[0024] For enabling a cyclic operation of the system, the lean (regenerated) solvent obtained after desorption of CO2 in the desorption container, can be circulated back to an absorption container for reutilization of its CO2 absorbing properties. The absorption container is configured to receive the exhaust gas comprising CO2 from the large engine and a non-CO2 comprising (lean) solvent, wherein the lean solvent absorbs at least a part of the CO2 from the exhaust gas, thereby producing CO2 comprising ‘rich’ solvent and exhaust gas having a reduced CO2 content. The CO2 comprising ‘rich’ solvent can be supplied to the system of the invention for CO2 desorption.

[0025] Further, according to the invention, the system comprises a low-pressure source in a fluid connection with the desorption container which is configured in such a way that the low- pressure (e.g. in the range of -550 mbar to -300 mbar) generated by the low-pressure source enhances the evaporation of the CO2 comprising fluid from the rich solvent in the desorption container.

[0026] Herein, the term “enhances” comprises an improved CO2 desorption process from the solvent (e.g. faster, more efficient, with more yield) as well as a CO2 desorption process at conditions at which normally a CO2 desorption would not be reasonably possible (e.g. at a temperature in the range of 7O-ioo°C instead of 12O-13O°C without the reduced pressure). This enables the desorption and therefore a CO2 separation from the exhaust gas of the large engine at a wider range of operating conditions such as a lower engine load where, e.g. not enough waste heat is available for CO2 desorption without burning additional fuel for the desorption process. This leads to an overall increased CO2 separation potential which has a beneficial impact on the greenhouse gas footprint.

[0027] With the system of the invention, the desorption of CO2 from the solvent can be achieved at lower pressure and lower temperature conditions inside the desorption container. In particular, the temperature can be lower than 120-130 °C, which temperature is typically used for CO2 desorption. This leads to an overall increased CO2 capturing yield as a higher amount of CO2 can be captured in times of lower engine loads which would - without the invention - not provide enough waste heat for CO2 desorption / capturing.

[0028] Typically, the exhaust gas from large engines contains various components such as soot, particulate matter (PM), sulfur oxides (SOx), nitrogen oxides (NOx), and other gases besides carbon dioxide (CO2). These additional gases should be initially removed from the exhaust gas stream before initiating the carbon capture process in the system described herein. This step can be crucial to avoid degradation of the solvent and to maximize its CO2 absorption potential.

[0029] After the optional initial exhaust gas cleaning step, the cleaned exhaust gas stream can be introduced into a Direct Contact Cooler (DCC) to lower its temperature to, e.g. 4O°C. This cooling step thermodynamically favors the absorption of CO2 by the solvent. The cleaned and cooled exhaust gas stream can then be introduced into the absorption container. In the absorption container, under favorable thermodynamic conditions, a countercurrent flow of the CO2 and the lean solvent may be arranged which leads to the absorption of CO2 by the solvent. The rich solvent from the absorption container may then be transferred to the desorption container through the first transfer line.

[0030] According to an embodiment, the solvent is configured or selected such that it can absorb the CO2 from the exhaust gas in an exothermic reaction (absorption process) and that it can desorb the CO2 in an endothermic reaction (desorption process). Thus, the absorption and desorption processes enable cyclic CO2 absorption from the exhaust gas and CO2 desorption from the solvent. The solvent can thus be circulated in a closed circuit which leads to improved handling and can also be used to exchange heat between different stages of the solvent circulation, without additional energy expenditure. In addition, this also helps with maintenance of the whole system and enables cyclic operation.

[0031] Advantageously, the solvent is selected from a group consisting of Monoethanolamin (MEA), Diethanolamine (DEA), Methyldiethanolamine (MDEA), Piperazine (PZ), 2-Amino-2-methyl- 1-propanol (AMP), Potassium Carbonate and any of its promoted blends, Diglycolamine (DGA), Functionalized Ionic Liquids, Organic Solvents such as N-Methyl-2-pyrrolidone (NMP), Aqueous Ammonia, Sterically Hindered Amines such as 2-Amino-2-methylpropanol, Aminosilicones, Amine-Functionalized Polymers, and Solid Sorbents such as Metal-Organic Frameworks (MOFs), Zeolites or Activated Carbon, Amine-functionalized silica or alumina. A combination of two or more substances is possible as well.

[0032] According to another embodiment, the low-pressure source comprises a compressor that is connected to the desorption container, e.g., via a tube or a piping, in such a way that the low- pressure is generated in the desorption container. This leads to an improved desorption process and solvent regeneration.

[0033] According to an embodiment, the compressor connected to the desorption container is driven by exhaust gas of the large engine. This can be achieved by directing at least a (adjustable) part of the exhaust gas through a turbine connected to the compressor, which in turn drives the compressor. The compressor can be driven by a turbine of the main turbocharger of the large engine that is also used for charging the large engine. Then, the compressor can be coaxially connected to the main turbocharger.

[0034] Alternatively, the low-pressure source can comprise a secondary or an auxiliary turbine connected to the desorption container, which is not used to drive the main turbocharger for charging the large engine and is separate from the main turbocharger of the large engine. Then, only a part of the exhaust gas from the large engine is used to drive the auxiliary turbine.

[0035] Other possibilities for driving the compressor include an electric motor powered, e.g. by onboard electrical grids, a mechanical power take-off from the large engine, and a hydraulic system of the large engine.

[0036] According to an embodiment, the low-pressure source comprises a valve having a first inlet for the evaporated CO2 comprising fluid and a second inlet for a second fluid, wherein the second fluid comprises a motive gas or a liquid stream. The second inlet comprises a nozzle to accelerate the second fluid. An outlet of the valve combines the evaporated CO2 comprising fluid and the second fluid such that a low-pressure of, e.g. around 0.5-0.7 bars is generated in the evaporated CO2 comprising fluid and therefore in the desorption container.

[0037] According to an embodiment, the first inlet of the valve at least partially encircles the second inlet and the outlet comprises a diffuser. This leads to improved flow conditions. According to an embodiment, the system comprises a heat source configured to heat the rich solvent in the desorption container for evaporating the CO2 comprising fluid from the rich solvent. In an embodiment, the heat source comprises a heat pump for heating the solvent. In an embodiment, the solvent in the desorption container may be heated using an external heater, e.g. a combustion based heater, or a reboiler.

[0038] In a further embodiment, a cooler is connected to the desorption container and is configured to cool the evaporated CO2 comprising fluid and in particular configured to condense and separate evaporated water and solvent remains included in the evaporated CO2 comprising fluid. By means of the cooler, condensed solvent can be returned to the absorption container for re-circulation while the resulting CO2 comprising fluid can be further processed to extract purified or substantially pure CO2, which can be cooled and compressed to liquify and can be stored in a container under pressure for transportation to the destination harbor.

[0039] According to an embodiment, the system comprises a heat exchanger for transferring heat from the lean solvent in the second line to the rich solvent in the first line. This helps to save energy.

[0040] The first and second transfer lines between the absorption and desorption containers may form part of the heat exchanger. In the heat exchanger, heat from the lean solvent in the second line is transferred to the rich solvent in the first line, thereby raising the temperature of the rich solvent entering the desorption container and lowering the temperature of the lean solvent from the system.

[0041] According to an embodiment the system comprises means for intermediate storage of heat from the engine, wherein the means for intermediate storage of heat is connected to the desorption container to provide heat to the CO2 comprising solvent received therein. The heat storage means maybe used for storing heat from exhaust gas of the large engine operation at higher loads. In particular, the means for intermediate heat storage comprise a latent heat storage material that undergoes a phase-change in the relevant temperature range. This helps to increase the operational efficiency.

[0042] According to an embodiment, the low-pressure source is directly connected to the desorption container. This helps to simplify the system.

[0043] According to an embodiment the system further comprises means for intermediate solvent storage, wherein the means for intermediate solvent storage is configured to, at a first time, store rich solvent, and at a second time, supply the stored rich solvent to the desorption container. A time interval between the first time and the second time is preferably at least 5 minutes, more preferably at least 15 minutes, and advantageously at least 30 minutes.

[0044] According to a second aspect of the invention, a method for separating CO2 from an exhaust gas of a large engine (11), in particular on board of a marine vessel, by means of a solvent (3) is provided. The solvent is capable of reversibly absorbing CO2 from the exhaust gas to generate rich solvent and capable of desorbing a CO2 comprising fluid to regenerate lean solvent. The method involves receiving the exhaust gas comprising CO2 from the large engine and lean solvent in an absorption container, wherein the lean solvent absorbs at least a part of the CO2 from the exhaust gas, thereby producing rich solvent and exhaust gas having a reduced CO2 content, supplying rich solvent from the absorption container (13) to a desorption container, applying a low pressure to the rich solvent in the desorption container, and evaporating the CO2 comprising fluid from the rich solvent under the low pressure in a desorption process to generate lean solvent. According to the method a desorption of CO2 from the solvent can be achieved at lower pressure and lower temperature conditions which can help to increase the overall CO2 capturing capabilities.

[0045] According to the invention, the method comprises a further step of supplying non-CO2 comprising solvent or lean solvent from the desorption container to the absorption container. The absorption process may by conducted in a countercurrent arrangement of the lean solvent and the exhaust gas streams.

[0046] According to an embodiment, the method further includes heating the rich solvent in the desorption container to a temperature within a range of, e.g. 7O-1OO°C for the desorption process.

[0047] According to an embodiment, the method further includes decreasing the pressure inside the desorption container to a range of, e.g. 0.45 - 0.7 bars to facilitate or enhance the desorption process. A low-pressure source, such as a compressor or a vacuum pump or an auxiliary turbine, can be connected to the desorption container to enhance the evaporation of the CO2 comprising fluid from the rich solvent.

[0048] When the heat exchange between the lean and rich solvents is not sufficient to raise the temperature of the solvent inside the desorption container to enable CO2 evaporation conditions, an intermediate storage of heat from the engine can be connected to the desorption container to provide additional heat to the rich solvent received therein. According to an embodiment, the method comprises a further step of cooling the evaporated CO2 comprising fluid (e.g. by means of a cooler connected to the desorption container), a step of condensing and separating evaporated water and solvent remains included in the evaporated CO2 comprising fluid, and a further step of compressing resulting CO2 to liquify the CO2 from the evaporated CO2 comprising fluid for further storage and / or treatment.

[0049] As a third aspect of the invention, a propulsion system for a marine vessel includes a large engine and a system for separating CO2 from the exhaust gas of the large engine, configured as described above. The method and system described herein can be used in a longitudinally scavenged two-stroke engine with at least one cylinder having an inner diameter of at least 200 mm. Thus, the CO2 content of the large engine can be considerably reduced which is beneficial for protection of our climate.

[0050] According to a fourth aspect of the invention, use of a vacuum ejector, i.e. a valve having a first inlet for the evaporated CO2 comprising fluid and a second inlet for a second fluid, wherein the second inlet comprises a nozzle to accelerate the second fluid, wherein an outlet of the valve combines the evaporated CO2 comprising fluid and the second fluid for generating a low- pressure in a desorption container of a system as describe above with regard to the first aspect is disclosed.

[0051] Brief Description of the Drawings

[0052] The invention will be better understood and objects other than those set forth above will become apparent when consideration is given to the following detailed description thereof. Such description refers to the annexed drawings, wherein:

[0053] FIG. 1 illustrates a system comprising a CO2 absorption container and a corresponding desorption container in accordance with an embodiment of the present invention;

[0054] FIG. 2 illustrates an embodiment of a low pressure source in accordance with a further embodiment of the present invention, to generate a low-pressure inside the desorption container; and

[0055] FIG. 3 shows a schematic representation of an embodiment of a large engine.

[0056] Figure 1 shows an on-board chemical absorption carbon capture system for use on board of a marine vessel according to an embodiment of the present invention. The system comprises an apparatus 27 configured for CO2 desorption from a solvent 3 supplied to a desorption container 1 of the apparatus 27. Preferably, the solvent 3 is capable of reversibly absorbing and desorbing CO2 from an exhaust gas 15 of a large engine 11 of the vessel. An example of the large engine 11 is shown in more detail in Fig. 3.

[0057] The system comprises a Direct Contact Cooler (DCC) unit 2 which is configured to receive filtered exhaust gas 15 from the large engine 11 through a heat exchanger 26 to reduce its temperature. The exhaust gas 15 includes CO2 and its temperature is further reduced to around 4O°C by a cooler 4 of the DCC unit 2 to enhance absorption of CO2 from the exhaust gas by the solvent 3.

[0058] To carry out the absorption process the cooled exhaust gas 15 comprising CO2 is supplied from the DCC unit 2 to the absorption container 13 and a non-CO2 comprising or lean solvent 3 is also supplied to the absorption container 13 at an upper portion thereof after a cooling process in a cooler 28. In the absorption container 13 the non-CO2 comprising solvent 3 absorbs at least a part of the CO2 from the exhaust gas 15 in a countercurrent process, thereby producing CO2 comprising or rich solvent 3. This absorption process reduces the amount of CO2 in the exhaust gas 15. The absorption of CO2 by the lean solvent 3 is an exothermic reaction resulting in a temperature increase of the CO2 rich solvent. The purified and CO2 depleted exhaust gas 15 is exhausted from the absorption container 13 through an outlet provided at the top (“clean gas”). Before reaching the outlet, the exhaust gas 15 is further cleaned in a water wash effected by spraying water inside the absorption container 1 at a top portion thereof as is visible in Fig. 1. This is done in order to reduce the emissions of volatile compounds into the atmosphere.

[0059] The absorption container 13 is connected to the desorption container 1 by a first transfer line 14 configured to transfer the CO2 comprising solvent 3 to the desorption container 1.

[0060] The desorption container 1 is configured to receive the CO2 comprising solvent 3 and to evaporate a CO2 comprising fluid from the CO2 comprising solvent 3 in the container 1 in a desorption process such that non-CO2 comprising solvent 3 or lean solvent is generated.

[0061] The non-CO2 comprising solvent from the desorption container 1 is transferred back to the absorption container 13 via a second transfer line 16. The first and second transfer lines 14, 16 are connected to a common heat exchanger 6 so that lean solvent 3 from the desorption container 1 is cooled and rich solvent from the absorption container 13 is heated. A low-pressure source 5 in a fluid connection with the desorption container 1 is configured such that the low-pressure generated by the low-pressure source 5 enhances the evaporation of the CO2 comprising fluid from the rich solvent 3 in the desorption container 1.

[0062] In the embodiment shown in figure 1, the low-pressure source 5 comprises a compressor 7 that is connected to the desorption container 1 in such a way that the low-pressure is generated in the desorption container 1. The compressor 7 maybe connected to desorption container 1 by a pipe that is mounted to a top part of the desorption container 1. Various means can be used to drive the compressor 7.

[0063] According to the given embodiment shown in Fig. 1, the compressor 7 is driven by exhaust gas 15 of the large engine 11, wherein at least a part of the exhaust gas 15 is directed through an auxiliary turbine 10 connected to the compressor 7 and thereby drives the compressor 7. After passing through the auxiliary turbine 10 the exhaust gas 15 is recombined with the mainstream of exhaust gas 15 from the large engine 11 and subsequently directed through the heat exchanger 26.

[0064] According to an alternative, as shown in figure 1 by the dashed line, a main turbocharger 9 of the large engine 11 that is also used for charging the large engine 11 is, for example, mechanically connected to the compressor 7 and the compressor 7 is driven by the main turbocharger 9.

[0065] Figure 1 further shows a cooler 12 connected to the desorption container 1 downstream the compressor 7 which is configured to cool the evaporated CO2 comprising fluid and configured to condense and separate evaporated water and solvent 3 remains included in the evaporated CO2 comprising fluid. The separated CO2 is then further processed, purified and compressed to liquify and store in one or more appropriate containers. For this purpose, additional compressor and cooling stages 25 are provided downstream the cooler 12. The solvent 3 is reintroduced into the desorption container 1 after the removal of CO2.

[0066] To enhance the desorption process of the CO2 comprising fluid from the desorption container 1, the heat recovered from the exhaust gas 15 by the heat exchanger 26 is used for heating the desorption container 1. However, the amount of heat provided to the desorption container 1 depends on the temperature of the exhaust gas 15 of the large engine 11. The temperature of the exhaust gas 15 can, e.g. only be sufficient to heat the rich solvent 3 in the desorption container 1 to a temperature of 12O-13O°C in the desorption container 1 that is sufficient for the evaporation of a significant amount of CO2 comprising fluid if the large engine runs at its full load capacity. In contrast, the evaporation of the CO2 comprising fluid will not be sufficient to desorb a significant amount of CO2 in situations where the large engine 11 runs at low loads, e.g. at 50% load or less. According to the present invention, the evaporation rate of the CO2 comprising fluid is enhanced by generating low pressure with the low-pressure source 5 connected, in particular directly connected without any active components such as tanks, separators and similar inbetween, to the desorption container 1. Preferably, the evaporation rate of the CO2 comprising fluid at lower solvent temperatures in the range of 7O-1OO°C is thus enhanced, e.g. to an amount comparable to evaporation conditions when the large engine 11 is running at its full capacity.

[0067] Figure 2 illustrates an alternative low-pressure source 5. This low-pressure source may replace or supplement the compressor 7 shown in Fig. 1 and can be connected to the desorption container to generate a low-pressure inside the desorption container 1. This low-pressure source 5 comprises a valve 20 having a first inlet 17 for the evaporated CO2 comprising fluid from the desorption container 1 and a second inlet 19 for a second fluid. The first inlet 17 of the valve 20 at least partially encircles the second inlet 19. Furthermore, the outlet 23 comprises a diffuser 18. The second inlet 19 comprises a nozzle 21 which accelerates the second fluid. The outlet 23 of the valve 20 combines the evaporated CO2 comprising fluid and the accelerated second fluid such that in combination with the diffuser 23 a low-pressure is generated in the evaporated CO2 comprising fluid the desorption container 1 so that the amount of evaporated CO2 comprising fluid is increased even at lower temperatures in the range of 7O-1OO°C of the solvent in the desorption container 1 instead of 12O-13O°C of the solvent 3 which can be achieved under conditions of the large engine 11 running at its full capacity.

[0068] Fig. 3 shows a schematic representation of an embodiment of a large engine 11 in cross-section. In Fig. 3, only one of the cylinders 110 of the large engine 11 is shown. Usually, the large engine 11 comprises a plurality of cylinders 110, for example at least four and up to twelve cylinders 110 or even more. The term "large engine" refers to internal combustion engines that are typically used as drive units for ships or in stationary operations, such as driving large generators for generating electrical energy. Typically, the cylinders 110 of a large engine 11 each have an inner diameter (bore) of at least about 200 mm. Large engines 11 are known in various configurations, for example as two-stroke engines or four-stroke engines.

[0069] In the following description, reference is made by way of example to a large engine 11 configured as a longitudinally scavenged two-stroke large engine having a plurality of cylinders 110. Each cylinder 110 has a combustion chamber too. Furthermore, in each cylinder 110, a piston 120 is arranged for reciprocating movement between a top dead center and a bottom dead center. The term "longitudinally scavenged" means that the scavenging or charging air is introduced into the cylinder 110 in the area of the lower end, and an exhaust valve 130 is arranged in or at the cylinder cover 32 located at the upper end of the cylinder 110.

[0070] In particular, reference is made to a large longitudinally scavenged two-stroke engine that can be operated with different fuels, namely with a first fuel and with a second fuel. Preferably, the large engine 11 is configured as a large diesel engine. The term "large diesel engine" refers to engines that can be operated at least in diesel operation. In particular, the term "large diesel engine" also comprises large engines 11 that can be operated in another mode, e.g., Otto operation, in addition to diesel operation.

[0071] According to a preferred configuration, the large engine 11 can be operated with methanol or ammonia as a first fuel and with a self-igniting and liquid second fuel. For this, the large engine 11 comprises a first fuel supply system and a second fuel supply system. Usually, liquid fuel, such as heavy fuel oil (HFO), marine diesel oil (MDO), or marine gas oil (MGO), is injected directly into the combustion chamber 100 at a suitable time and ignites there according to the diesel principle of self-ignition. For injecting the second fuel into the combustion chamber 100, each cylinder comprises a second fuel injector 150, which is different from the first fuel injector 33. Thus, each cylinder 110 comprises at least one, but preferably a plurality of, first fuel injectors 33 for injecting the first fuel, as well as at least one, but preferably a plurality of, second fuel injectors 150 for injecting the second fuel.

[0072] The first fuel, which is injected with the fuel injector 33 into the combustion chamber 100, is, for example, a fuel for Otto operation, i.e., with induced ignition of the fuel. The first fuel can be injected into the combustion chamber 100 where it is ignited according to the Otto principle. This induced ignition is usually caused by introducing a small amount of self-igniting second fuel (e.g., diesel or heavy fuel oil) into the combustion chamber 100 or into a pre-chamber at a suitable moment, which second fuel then ignites itself and causes the induced ignition of the first fuel in the combustion chamber 100.

[0073] Introducing a small amount of a self-igniting liquid second fuel into the combustion chamber 100 or into at least one pre-chamber for the induced ignition of the first fuel is also referred to as pilot ignition. Beside a diesel oil it is also possible to use a gas or an alcohol such as methanol as pilot fluid for the pilot ignition.

[0074] In other embodiments, the induced ignition is achieved by way of spark ignition, laser pulse, or any other means suited for igniting the fuel in the combustion chamber 100. In the following description, reference is made to a preferred embodiment in which the first fuel is methanol or ammonia, and the second fuel is a diesel fuel for self-ignition, for example HFO, MDO, or MGO. Regarding the first fuel, it is preferred that the operation with the first fuel is an operation according to the Otto principle.

[0075] Furthermore, the large diesel engine 11 can be operated in a mixed mode, in which both the first fuel and the second fuel are injected into the combustion chamber too of the cylinder no. In the mixed mode, both the combustion of the first fuel and the combustion of the second fuel contribute to the generation of torque.

[0076] In the embodiment described here, the large engine is configured as a longitudinally scavenged dual-fuel two-stroke large diesel engine, which can be operated with methanol or ammonia as the first fuel and / or with a diesel fuel as the second fuel.

[0077] The dual-fuel large diesel engine has a plurality of cylinders no. In each cylinder no, the piston 120 is connected in a manner known per se to a crosshead 122 via a piston rod 121. The crosshead 122 is connected to a crankshaft 170 via a push rod or connecting rod 123, so that the movement of the piston 120 is transmitted via the piston rod 121, the crosshead 122, and the connecting rod 123 to the crankshaft 170 to rotate it. The upper side of the piston 120, together with the cylinder cover 2, delimits the combustion chamber 100 into which the first fuel and / or the second fuel is introduced.

[0078] The structure and individual components of a large diesel engine 11, such as the injection system for the fuels, the gas exchange system, the exhaust system, the turbocharger system for the supply of scavenging or charging air, as well as the monitoring and control system, are sufficiently known to those skilled in the art for both two-stroke and four-stroke engine designs and therefore need no further explanation here.

[0079] In the embodiment of a longitudinally scavenged two-stroke large diesel engine 11, scavenging air slots 115 are usually provided in the lower region of each cylinder 110 or cylinder liner. These slots are periodically closed and opened by the movement of the piston 120 in the cylinder 110, allowing the scavenging air provided by the main turbocharger 9 under charging pressure to flow into the cylinder 110 through the scavenging air slots 115 when they are open. In the cylinder cover 32, the usually centrally arranged exhaust valve 130 is provided, through which the exhaust gases can be discharged from the cylinder 110 into the exhaust system after the combustion process. The exhaust system guides at least a part of the exhaust gases to a turbine of the main turbocharger 9, whose compressor provides the scavenging air, also referred to as charging air, in a scavenge air receiver under scavenge air pressure. The scavenge air receiver is in fluid communication with the scavenging air slots 115 of the cylinders 110.

[0080] Each cylinder 110 comprises at least one first fuel injector 33 for injecting the first fuel into the combustion chamber 100 of the cylinder 110. Preferably, the cylinder 110 comprises a plurality of first fuel injectors 33, for example two or three first fuel injectors 33, for uniformly distributing the first fuel in the combustion chamber 100. In the embodiment of the large engine 11 described here, exactly three first fuel injectors 33 are provided (only one first fuel injector 33 is shown in the schematic representation of Fig. 3). Each first fuel injector 33 is arranged in the cylinder cover 32 of the cylinder 110. The cylinder cover 32 comprises an inner surface for delimiting the combustion chamber too and an injector bore extending through the cylinder cover 32 and opening into the inner surface. The injector bore is configured to receive the first fuel injector 33. Preferably, the first fuel injectors 33 are arranged in the cylinder cover 32 near the exhaust valve 130.

[0081] Each cylinder 110 further comprises at least one second fuel injector 150 for injecting the second fuel into the combustion chamber too of the cylinder 110. Preferably, the cylinder 110 comprises a plurality of second fuel injectors 150, for example two or three second fuel injectors 150, for uniformly distributing the second fuel in the combustion chamber too. In the embodiment of the large engine 200 described here, exactly three second fuel injectors 150 are provided (only one second fuel injector 150 is shown in the schematic representation of Fig. 3). Each second fuel injector 150 is arranged in the cylinder cover 32 of the cylinder 110 in a manner known in the art. Preferably, the second fuel injectors 150 are arranged in the cylinder cover 32 near the exhaust valve 130.

[0082] Nowadays, a large diesel engine or a large engine 11 in general is operated in a fully electronically controlled manner. An engine control unit 180 operates and controls all functions of the large engine 11— for example, the operation of the exhaust valves 130 for the gas exchange, the injection process for the fuels, and the pilot injection timing (when pilot injection is required)— by way of electric or electronic signals and commands. In addition, the engine control unit 180 receives information from several detectors, sensors, or measuring devices.

[0083] It is noted that the invention is not restricted to this specific type of a longitudinally scavenged two-stroke large engine 11, which can be operated with the first fuel and / or with the second fuel. The large engine can also be any other type of large engine. In particular, it is possible that the large engine is configured for the combustion of only one fuel. Further embodiments of the invention are disclosed by the following clauses:

[0084] 1. An apparatus configured for CO2 desorption from a solvent (3), wherein the solvent (3) is capable of reversibly absorbing and desorbing CO2 from an exhaust gas of a large engine (11), the apparatus comprising: a desorption container (1) configured to receive a CO2 comprising solvent (3), wherein the desorption container (1) is configured to evaporate a CO2 comprising fluid from the CO2 comprising solvent (3) in the container (1) in a desorption process such that a non-CO2 comprising solvent (3) is generated, and a low-pressure source (5) in a fluid connection with the desorption container (1), configured such that a low-pressure generated by the low-pressure source (5) enhances the evaporation of the CO2 comprising fluid from the CO2 comprising solvent (3) in the desorption container (1).

[0085] 2. The apparatus of clause 1 wherein the solvent (3) is configured to absorb CO2 from the exhaust gas in an exothermic absorption process and wherein the solvent (3) is further configured to desorb CO2 in an endothermic desorption process, such that the absorption and desorption processes enable a cyclic CO2 absorption from the exhaust gas and CO2 desorption from the solvent (3).

[0086] 3. The apparatus of any one of the preceding clauses, wherein the low-pressure source (5) comprises a compressor (7) that is connected to the desorption container (1) in such a way that the low-pressure is generated in the desorption container (1).

[0087] 4. The apparatus of clause 3, wherein the compressor (7) is driven by exhaust gas of the large engine (11), wherein at least a part of the exhaust gas is directed through a turbine (9) connected to the compressor (7) and thereby drives the compressor (7), and in particular wherein the compressor (7) is driven by at least one of the group of a main turbocharger turbine of the large engine (11) that is also used to drive a main turbocharger for charging the large engine (11), an auxiliary turbine separate from a main turbocharger turbine of the large engine (11), which auxiliary turbine is not used to drive the main turbocharger, and wherein only a part of the exhaust gas from the large engine is used to drive the auxiliary turbine, and in particular wherein the part of the exhaust gas that drives the auxiliary turbine is adjustable, preferably based on an engine parameter such as an engine load, an electric motor, a mechanical power take-off from the large engine, and a hydraulic system of the large engine. The apparatus of any one of the preceding clauses, wherein the low-pressure source (5) comprises a valve (15) having a first inlet (17) for the evaporated CO2 comprising fluid and a second inlet (19) for a second fluid, wherein the second inlet (19) comprises a nozzle (21) to accelerate the second fluid, wherein an outlet (23) of the valve (15) combines the evaporated CO2 comprising fluid and the second fluid such that the low- pressure is generated in the desorption container (1). The apparatus of clause 5, wherein the first inlet (17) of the valve (15) at least partially encircles the second inlet (19) and wherein the outlet (23) comprises a diffuser (18). The apparatus of any one of the preceding clauses, comprising a heat source configured to heat the CO2 comprising solvent (3) in the desorption container (1) for evaporating the CO2 comprising fluid from the CO2 comprising solvent (3), and in particular wherein the heat source comprises a heat pump or a combustion-based heater. The apparatus of any one of the preceding clauses, comprising a cooler (12) connected to the desorption container (1) and configured to cool the evaporated CO2 comprising fluid and in particular configured to condense and separate evaporated water and solvent (3) remains included in the evaporated CO2 comprising fluid. A system for separating CO2 from an exhaust gas of a large engine (11), in particular configured for use on board of a marine vessel, the system comprising: an absorption container (13) configured to receive the exhaust gas (15) comprising CO2 from the large engine (11) and a non-CO2 comprising solvent (3), wherein the non-CO2 comprising solvent (3) absorbs at least a part of the CO2 from the exhaust gas (15), thereby producing CO2 comprising solvent (3) and exhaust gas having a reduced CO2 content, and an apparatus of any one of the preceding clauses for desorbing a CO2 comprising fluid from the CO2 comprising solvent (3), thus regenerating the non-CO2 comprising solvent (3), wherein the absorption container (13) is connected to the apparatus by a first line (14) configured to transfer the CO2 comprising solvent (3) to the apparatus. The system of clause 9, further comprising a second line (16) connecting the apparatus with the absorption container (13), the second line (16) being configured to transfer the non-CO2 comprising solvent (3) from the apparatus back to the absorption container (13), and in particular wherein the system further comprises a heat exchanger (6) for transferring heat from the non-CO2 comprising solvent in the second line (16) to the CO2 comprising solvent in the first line (14). The system of any one of the clauses 9 to 10, further comprising means for intermediate heat storage from the engine (11), wherein the means for intermediate heat storage is connected to the desorption container (1) to provide heat to the CO2 comprising solvent (3) received therein, and in particular wherein the means for intermediate heat storage comprises a latent heat storage material that undergoes a phase-change. A method for desorbing CO2 from a solvent (3), wherein the solvent (3) is capable of reversibly absorbing CO2 from an exhaust gas of a large engine (11), thus generating a CO2 comprising solvent (3) and capable of desorbing a CO2 comprising fluid from the CO2 comprising solvent (3) to regenerate a non-CO2 comprising solvent (3), the method comprising steps of: supplying the CO2 comprising solvent (3) to a desorption container (1); applying a low-pressure to the CO2 comprising solvent (3) in the desorption container (1); and evaporating the CO2 comprising fluid from the CO2 comprising solvent (3) under the low-pressure in a desorption process and thereby regenerating the non-CO2 comprising solvent (3), wherein the low-pressure enhances the evaporation of the CO2 comprising fluid from the CO2 comprising solvent (3) in the desorption container (1). The method of clause 12, comprising a further step of: supplying the non-CO2 comprising solvent (3) and the exhaust gas to an absorption container (13), wherein the non-CO2 comprising solvent (3) absorbs at least a part of the CO2 from the exhaust gas, thereby producing the CO2 comprising solvent (3) and exhaust gas having a reduced CO2 content. The method of any one of the clauses 12 or 13, comprising a further step of: heating the CO2 comprising solvent (3) in the desorption container (1) to a temperature within a range of 7O-1OO°C for the desorption process and / or decreasing the pressure inside the desorption container (1) to a range of 0.45 - 0.7 bars. The method of any one of the clauses 12-14, comprising further steps of: cooling the evaporated CO2 comprising fluid, condensing and separating evaporated water and solvent (3) remains included in the evaporated CO2 comprising fluid, and compressing resulting CO2 to liquify the CO2 for further storage and / or treatment.

[0088] 16. A propulsion system for a marine vessel comprising a large engine (n), in particular a longitudinally scavenged two-stroke engine with at least one cylinder having an inner diameter of at least 200 mm, and a system for separating CO2 from an exhaust gas of the large engine (11) according to any one of the clauses 9-11.

[0089] Any embodiments described with respect to the devices shall similarly pertain to the method. Synergetic effects may arise from different combinations of the embodiments although they might not be described in detail. While there are shown and described presently preferred embodiments of the invention, it is to be distinctly understood that the invention is not limited thereto but may be otherwise variously embodied and practiced within the scope of the following claims.

[0090] Reference numerals:

[0091] 1- desorption container

[0092] 2- Direct Contact Cooler (DCC) unit

[0093] 3- solvent

[0094] 4- cooler of the DCC unit

[0095] 5- low-pressure source

[0096] 6- heat exchanger

[0097] 7- compressor

[0098] 9- main turbocharger

[0099] 10- auxiliary turbocharger

[0100] 11- large engine

[0101] 12- cooler

[0102] 13- absorption container

[0103] 14- first line

[0104] 15- exhaust gas

[0105] 16- second line

[0106] 17- first inlet

[0107] 18- diffuser

[0108] 19- second inlet

[0109] 20-valve

[0110] 21- nozzle

[0111] 23- outlet

[0112] 25- compressor and cooling stages

[0113] 26- heat exchanger

[0114] 27- desorption apparatus

[0115] 32- cylinder cover

[0116] 33- first fuel injector too- combustion chamber 110- cylinder

[0117] 115- scavenging air slots

[0118] 120- piston

[0119] 121- piston rod

[0120] 122- crosshead

[0121] 123- connecting rod

[0122] 130- exhaust valve

[0123] 150- second fuel injector

[0124] 170- crankshaft i8o- engine control unit

Claims

WinGD Ltd.W32172WOClaims:

1. A system for separating CO2 from an exhaust gas of a large engine (11) by means of a solvent (3) which is capable of reversibly absorbing CO2 from the exhaust gas to generate rich solvent (3) and capable of desorbing a CO2 comprising fluid to regenerate lean solvent (3), wherein the system is in particular configured for use on board of a marine vessel, the system comprising: an absorption container (13) configured to receive the exhaust gas (15) comprising CO2 from the large engine (11) and lean solvent (3), wherein the lean solvent (3) absorbs at least a part of the CO2 from the exhaust gas (15), thereby producing rich solvent (3) and exhaust gas having a reduced CO2 content; a desorption container (1) configured to receive rich solvent (3) from the absorption container (13), wherein the desorption container (1) is configured to evaporate the CO2 comprising fluid from the rich solvent (3) in a desorption process such that lean solvent (3) is regenerated; a first line (14) connecting the absorption container (13) to the desorption container (1), the first line (14) being configured to transfer rich solvent (3) from the absorption container (13) to the desorption container (1); a second line (16) connecting the desorption container (1) to the absorption container (13), the second line (16) being configured to transfer lean solvent (3) from the desorption container (1) back to the absorption container (13); and a low-pressure source (5) in a fluid connection with the desorption container (1), configured such that a low-pressure generated by the low-pressure source (5) enhances the evaporation of the CO2 comprising fluid from the rich solvent (3) in the desorption container (1).

2. The system of claim 1 wherein the solvent (3) is configured to absorb CO2 from the exhaust gas in an exothermic absorption process and wherein the solvent (3) is further configured to desorb CO2 in an endothermic desorption process, such that the absorption and desorption processes enable a cyclic CO2 absorption from the exhaust gas and CO2 desorption from the solvent (3).

3. The system of any one of the preceding claims, wherein the low-pressure source (5) comprises a compressor (7) that is connected to the desorption container (1) in such a way that the low-pressure is generated in the desorption container (1).

4. The system of claim 3, wherein the compressor (7) is driven by exhaust gas of the large engine (11), wherein at least a part of the exhaust gas is directed through a turbine (9) connected to the compressor (7) and thereby drives the compressor (7), and in particular wherein the compressor (7) is driven by at least one of the group ofa main turbocharger turbine of the large engine (n) that is also used to drive a main turbocharger for charging the large engine (n), an auxiliary turbine separate from a main turbocharger turbine of the large engine (11), which auxiliary turbine is not used to drive the main turbocharger, and wherein only a part of the exhaust gas from the large engine is used to drive the auxiliary turbine, and in particular wherein the part of the exhaust gas that drives the auxiliary turbine is adjustable, preferably based on an engine parameter such as an engine load, an electric motor, a mechanical power take-off from the large engine, and a hydraulic system of the large engine.

5. The system of any one of the preceding claims, wherein the low-pressure source (5) comprises a valve (20) having a first inlet (17) for the evaporated CO2 comprising fluid and a second inlet (19) for a second fluid, wherein the second inlet (19) comprises a nozzle (21) to accelerate the second fluid, wherein an outlet (23) of the valve (20) combines the evaporated CO2 comprising fluid and the second fluid such that the low-pressure is generated in the desorption container (1).

6. The system of claim 5, wherein the first inlet (17) of the valve (20) at least partially encircles the second inlet (19) and wherein the outlet (23) comprises a diffuser (18).

7. The system of any one of the preceding claims, comprising a heat source configured to heat the rich solvent (3) in the desorption container (1) for evaporating the CO2 comprising fluid from the rich solvent (3), and in particular wherein the heat source comprises a heat pump or a combustionbased heater.

8. The system of any one of the preceding claims, comprising a cooler (12) connected to the desorption container (1) and configured to cool the evaporated CO2 comprising fluid and in particular configured to condense and separate evaporated water and solvent (3) remains included in the evaporated CO2 comprising fluid.

9. The system of any one of the preceding claims, further comprising a heat exchanger (6) for transferring heat from the lean solvent in the second line (16) to the rich solvent in the first line (14).

10. The system of any one of the preceding claims, further comprising means for intermediate heat storage from the engine (11), wherein the means for intermediate heat storage is connected to the desorption container (1) to provide heat to the rich solvent (3)received therein, and in particular wherein the means for intermediate heat storage comprises a latent heat storage material that undergoes a phase-change.

11. The system of any one of the preceding claims wherein the low-pressure source (5) is directly connected to the desorption container (1).

12. The system of any one of the preceding claims, further comprising means for intermediate solvent storage, wherein the means for intermediate solvent storage is configured to, at a first time, store rich solvent (3), and at a second time, supply the stored rich solvent to the desorption container (1).

13. A method for separating CO2 from an exhaust gas of a large engine (11), in particular on board of a marine vessel, by means of a solvent (3), wherein the solvent (3) is capable of reversibly absorbing CO2 from the exhaust gas to generate rich solvent (3) and capable of desorbing a CO2 comprising fluid to regenerate lean solvent (3), the method comprising steps of: receiving the exhaust gas comprising CO2 from the large engine (11) and lean solvent (3) in an absorption container (13), wherein the lean solvent (3) absorbs at least a part of the CO2 from the exhaust gas, thereby producing rich solvent (3) and exhaust gas having a reduced CO2 content; supplying rich solvent (3) from the absorption container (13) to a desorption container (1); applying a low-pressure to the rich solvent (3) in the desorption container (1); evaporating the CO2 comprising fluid from the rich solvent (3) under the low- pressure in a desorption process and thereby regenerating lean solvent (3), wherein the low-pressure enhances the evaporation of the CO2 comprising fluid from the rich solvent (3) in the desorption container (1); and supplying lean solvent (3) from the desorption container (1) to the absorption container (13).

14. The method of claim 13, comprising a further step of: heating the rich solvent (3) in the desorption container (1) to a temperature within a range of 7O-ioo°C for the desorption process.

15. The method of any one of the claims 13 to 14, comprising a further step of: decreasing the pressure inside the desorption container (1) to a range of 0.45 - 0.7 bars.

16. The method of any one of the claims 13 to 15, comprising further steps of: cooling the evaporated CO2 comprising fluid,condensing and separating evaporated water and solvent (3) remains included in the evaporated CO2 comprising fluid, and compressing resulting CO2 to liquify the CO2 for further storage and / or treatment.

17. A propulsion system for a marine vessel comprising a large engine (11), in particular a longitudinally scavenged two-stroke engine with at least one cylinder having an inner diameter of at least 200 mm, and a system for separating CO2 from an exhaust gas of the large engine (11) of any one of the claims 1-12.

18. A use of a valve (20) having a first inlet (17) for the evaporated CO2 comprising fluid and a second inlet (19) for a second fluid, wherein the second inlet (19) comprises a nozzle (21) to accelerate the second fluid, wherein an outlet (23) of the valve (20) combines the evaporated CO2 comprising fluid and the second fluid for generating a low-pressure in a desorption container (1) of a system of any one of the claims 1 to 12.

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