Method and installation for removing a gas from a flow of a gas mixture
A method and installation for removing a gas from a flow of a gas mixture. A first liquid ( 82 ) is introduced in the flow ( 106 ) for evaporative cooling and saturation of the gas mixture. Small droplets of a second liquid ( 84 ) are provided which are capable of adsorbing and dissolving said gas and of a size small enough not to be sedimented by gravitation and big enough to be centrifugally separated. The small droplets are sprayed into the flow for adsorbing and dissolving said gas into the droplets, and the small droplets are centrifugally separated from the flow.
1. A method of removing a gas from a flow of a gas mixture, characterized by:
introducing a first liquid in the flow for evaporative cooling and saturation of the gas mixture;
providing small droplets of a second liquid capable of dissolving said gas and of a size small enough not to be sedimented by gravitation and big enough to be centrifugally separated;
spraying the small droplets into the flow for adsorbing and dissolving said gas into the droplets; and
centrifugally separating the small droplets from the flow,
wherein the gas mixture is a combustion exhaust gas.
2. The method of claim 1 , comprising introducing the first liquid by spraying small droplets thereof into the flow.
3. The method of claim 2 , comprising forming the small droplets of the first liquid by atomization.
4. The method of claim 3 , comprising generating the atomization of the first liquid by pressurized air using a two-fluid nozzle or by high-pressure liquid spray using a single-fluid nozzle.
5. The method of claim 4 , comprising forming the small droplets of the second liquid by atomization.
6. The method of claim 5 , comprising generating the atomization of the second liquid by pressurized air using a two-fluid nozzle or by high-pressure liquid spray using a single-fluid nozzle.
7. The method of claim 2 , comprising controlling the size of the droplets of the first and second liquids to vary between 20 and 200 μm.
8. The method of claim 2 , comprising spraying the droplets of the second liquid downstream of spraying the droplets of the first liquid into the flow.
9. The method of claim 2 , comprising spraying the droplets of the second liquid co-currently with the flow.
10. The method of claim 1 , wherein the first liquid is water and the second liquid is an alkaline water solution.
11. The method of claim 1 , wherein the gas to be removed is a gas comprising sulphur oxides.
12. The method of claim 1 , wherein the gas mixture is an exhaust gas flow from a marine diesel engine and the gas to be removed is a gas comprising sulphur oxides.
13. The method of claim 1 , wherein the first liquid and the second liquid are introduced by spraying small droplets thereof into the flow by atomization, generating said atomization by pressurized air using a two-fluid nozzle or by high-pressure liquid spray using a single-fluid nozzle and further comprising controlling the size of the droplets of the first and second liquids to vary between 20 and 200 μm.
14. An installation ( 10 ) to be inserted in a path of an exhaust flow of an exhaust pipe ( 104 ) for performing the method of claim 10 , characterized by
spray nozzles ( 32 , 42 ) for the water and the alkaline water solution; and
at least one centrifugal separator ( 52 ) downstream of the spraying nozzles in the flow;
said spray nozzles comprising
at least one water spray nozzle ( 32 ); and
at least one atomizing spray nozzle ( 42 ) downstream of the at least one water spray nozzle ( 32 ) in the flow for producing the droplets of the alkaline solution.
15. The installation ( 10 ) of claim 14 , wherein the exhaust pipe ( 104 ) is an exhaust pipe of a marine diesel engine.
16. The installation of claim 14 or 15 , wherein the spray nozzles ( 32 , 42 ) are single fluid nozzles or two-fluid nozzles.
17. The installation of claim 14 , wherein the at least one spray nozzle ( 42 ) is oriented for spraying co-currently with the flow and the at least one spray nozzle ( 32 ) is oriented for spraying counter-currently with the flow.
18. The installation of claim 14 , comprising a control and actuation unit ( 80 ) capable of controlling the size of the droplets in dependence of engine load during operation.