Offshore processing method and system
A method for removal of a compound from a crude hydrocarbon gas stream to be obtained from a sub-sea well is disclosed. The method comprises bringing the crude hydrocarbon gas stream in contact with a treatment solution comprising an absorbent at least partly selective to the compound to be removed, thereby obtaining a rich treatment solution and a compound depleted gas stream, regenerating the treatment solution comprising the absorbent by desorbing the compound from the rich treatment solution, thereby obtaining a compound stream. The crude hydrocarbon gas stream is brought in contact with the treatment solution comprising the absorbent subsea, the compound depleted gas stream is obtained subsea, where as the regenerating of the rich treatment solution and obtaining the compound stream is performed topside Further a system for transporting a treatment fluid from a subsea treatment unit to a topside regeneration involving adding pressurized hot natural gas to the treatment fluid subsea as a lift gas and separating the natural gas from the treatment fluid topside before the treatment fluid enters the treatment unit is described.
1. A crude natural gas treatment system for removal of a compound from a crude natural gas stream, the system comprising:
an absorption unit which includes a natural gas inlet, a treatment solution inlet, a compound depleted gas outlet and a rich treatment solution outlet;
a desorption unit which includes a rich treatment solution inlet, a compound outlet and a depleted treatment solution outlet;
wherein the rich treatment solution outlet is in fluid communication with the rich treatment solution inlet and the depleted treatment solution outlet is in fluid communication with the treatment solution inlet;
wherein the absorption unit is located subsea and the desorption unit is located topside; and
a heat exchanger for heat exchanging the rich treatment solution with the depleted treatment solution;
wherein the heat exchanger is a pipe-in-pipe riser through which the rich treatment solution and the depleted treatment solution are conveyed.
2. The system according to claim 1 , wherein the pipe-in-pipe riser comprises an inner pipe in fluid communication with the depleted treatment solution outlet topside and the treatment solution inlet subsea, and an outer pipe in fluid communication with the rich treatment solution outlet subsea and the rich treatment solution inlet topside.
3. The system according to claim 1 , wherein the absorption unit comprises at least one of an in-line mixing device and a contactor column.
4. A crude natural gas treatment system for removal of a compound from a crude natural gas stream, the system comprising:
an absorption unit which includes a natural gas inlet, a treatment solution inlet, a compound depleted gas outlet and a rich treatment solution outlet; and
a desorption unit which includes a rich treatment solution inlet, a compound outlet and a depleted treatment solution outlet;
wherein the rich treatment solution outlet is in fluid communication with the rich treatment solution inlet and the depleted treatment solution outlet is in fluid communication with the treatment solution inlet;
wherein the absorption unit is located subsea and the desorption unit is located topside;
a second absorption unit which includes a second natural gas inlet, a second treatment solution inlet, a second compound depleted gas outlet and a second rich treatment solution outlet; and
a second desorption unit which includes a second rich treatment solution inlet, a second compound outlet and a second depleted treatment solution outlet;
wherein the second natural gas inlet is in fluid communication with the compound depleted gas outlet, the second rich treatment solution outlet is in fluid communication with the second rich treatment solution inlet, and the second depleted treatment solution outlet is in fluid communication with the second treatment solution inlet; and
wherein the second absorption unit is located subsea and the second desorption unit is located topside.
5. The system according to claim 4 , wherein the first compound is CO 2 , the absorption unit is a CO 2 absorber, the second compound is H 2 O and the second absorber is a dehydrator.