Gas compression system
US-9032987-B2 · May 19, 2015 · US
US10774822B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10774822-B2 |
| Application number | US-201816157212-A |
| Country | US |
| Kind code | B2 |
| Filing date | Oct 11, 2018 |
| Priority date | Dec 8, 2014 |
| Publication date | Sep 15, 2020 |
| Grant date | Sep 15, 2020 |
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A system and method for boosting the pressure of a low-pressure multiphase mixture into a high-pressure multiphase mixture. The system includes a gas-liquid separator, a liquids pump and a liquid piston compressor. The method includes introducing the low-pressure multiphase mixture into the pressure boost system, operating such that a low-pressure liquid and a low-pressure gas form, boosting the pressure of the low-pressure liquid to a high-pressure liquid, introducing low-pressure gas during a charging period into the liquid piston compressor, converting the low-pressure gas into high-pressure gas using the high-pressure liquid during a compression period, discharging the high-pressure gas form the liquid piston compressor, and mixing the high-pressure liquid and gas such that the high-pressure multiphase mixture.
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What is claimed is: 1. A method for boosting a pressure of a low-pressure multiphase mixture to a high-pressure multiphase mixture, the method comprising the steps of: introducing the low-pressure multiphase mixture into a pressure boost system, where the low-pressure multiphase mixture comprises a low-pressure liquid an a low-pressure gas; operating the pressure boost system such that the low-pressure liquid and the low-pressure gas form from the low-pressure multiphase mixture within a gas-liquid separator, a high-pressure liquid forms from the low-pressure liquid by a liquids pump that couples to a liquid portion of the gas-liquid separator, during a charging period the low-pressure gas is introduced into and the low-pressure liquid passes from a liquid piston compressor, during a compression period a high-pressure liquid is introduced into the liquid piston compressor such that the low-pressure gas converts into a high-pressure gas, during a discharging period the high-pressure liquid is introduced into and the high-pressure gas passes from the liquid piston compressor, a gas portion of the liquid piston compressor couples to a production line such that there is one-way fluid communication of high-pressure gas from the liquid piston compressor to the production line, and the liquids pump couples to the production line such that there is communication of the high-pressure liquid from the liquids pump to the production line that bypasses the liquid piston compressor, the high-pressure liquid and the high-pressure gas are mixed such that the high-pressure multiphase mixture forms; cooling the liquid piston compressor with a cooling system having an inlet head at a first end of the liquid piston compressor, an outlet head at an opposite end of the liquid piston compressor, and a shell fluid void located between the inlet head and the outlet head and within the liquid piston compressor, where the inlet head is in fluid communication with the liquid portion of the gas-liquid separator by way of a cooling liquid feed line and the outlet head is in direct fluid communication with the gas-liquid separator by way of a return line, where the low-pressure liquid passes through the cooling liquid feed line and returns to the gas-liquid separator to mix with the low-pressure multiphase mixture being introduced into the pressure boost system; and passing the high-pressure multiphase mixture from the pressure boost system. 2. The method of claim 1 where a pressure difference between the high-pressure liquid and the high-pressure gas is not substantial. 3. The method of claim 1 where the pressure boost system is operated such that the liquid piston compressor during the compression period is maintained at a substantially isothermal condition. 4. The method of claim 1 where the compression period starts at a detection of a low liquid level and ends at a detection of a high level liquid level within the liquid piston compressor. 5. The method of claim 1 where the charging period starts at a detection of a high liquid level and ends at a detection of a low level liquid level within the liquid piston compressor. 6. The method of claim 1 where during the compression period a cooling liquid is introduced to the liquid piston compressor by way of the cooling liquid feed line. 7. The method of claim 1 where during both the compression period and the discharge period a cooling liquid is introduced to the liquid piston compressor such that the liquid piston compressor is maintained at a substantially isothermal condition. 8. The method of claim 1 where the pressure boost system comprises more than one liquid piston compressor and where when a first liquid piston compressor is operating in the charging period a second liquid piston compressor is operating in the discharging period. 9. The method of claim 1 , where introducing the high-pressure liquid into the liquid piston compressor the liquid piston compressor includes introducing the high-pressure liquid into a plurality of liquid piston compressor tubes located within a shell. 10. The method of claim 9 , further including introducing a cooling liquid into the shell fluid void, where the shell fluid void is located inside the shell of the liquid piston compressor and is bound by an exterior surface of each of the plurality of liquid piston compressor tubes.
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