Use of hydraulic turbocharger for recovering energy from high pressure solvents in gasification and natural gas applications
The invention provides a process and system for regenerating a solvent used to remove carbon dioxide from feed gases, such as natural gas and synthesis gas. The invention employs one or more hydraulic turbochargers to transfer energy from a higher energy solvent stream to a lower energy solvent stream. This provides for a significant reduction in operating expenses.
1. A process for treating a carbon dioxide and/or hydrogen sulfide containing gas comprising:
a) sending a feed gas containing carbon dioxide and hydrogen sulfide through a carbon dioxide absorber unit or a hydrogen sulfide absorber unit or through a carbon dioxide absorber unit and a hydrogen sulfide absorber unit, wherein said carbon dioxide absorber unit and said hydrogen sulfide absorber unit contain a lean solvent to produce a loaded solvent containing a majority of said carbon dioxide and/or hydrogen sulfide from said feed gas and a treated gas;
b) regenerating said loaded solvent in a carbon dioxide and or hydrogen sulfide removal system;
c) recovering energy from at least one solvent stream to boost pressure of at least one other solvent stream wherein at least one hydraulic turbocharger is used to recover said energy from a solvent stream that exits said carbon dioxide and/or hydrogen sulfide absorber unit and transfers said energy to pump a semi-lean solvent stream from said carbon dioxide removal system; and
d) a second hydraulic turbocharger to recover energy from a hydrogen sulfide concentrator solvent stream to use in pumping a lean solvent stream.
2. A system for treating a carbon dioxide containing gas comprising a carbon dioxide absorber unit containing a lean solvent to produce a loaded solvent containing a majority of said carbon dioxide from carbon dioxide containing gas and a treated gas; a carbon dioxide removal system and at least one hydraulic turbocharger is used to recover energy from at least one solvent stream and to transfer said energy to a second solvent stream wherein a hydraulic turbocharger is used to recover energy from a semi-lean solvent stream that exits said carbon dioxide absorber unit and transfers said energy to pump a semi-lean solvent stream from said carbon dioxide removal system wherein a second hydraulic turbocharger to recover energy from a hydrogen sulfide concentrator solvent stream is used in pumping a lean solvent stream.
3. The system of claim 2 wherein said solvent is selected from the group consisting of dimethylether of polyethylene glycol, methanol, a mixture of N-formyl and N-acetyl morpholine, N-methyl-2-pyrrolidone and sulfolane.