Mitigating Liquid Carry-Over and Foaming in a Gas Processing Plant through the Installation of Vertical Scrubbers

Mitigating Liquid Carry-Over and Foaming in a Gas Processing Plant through the Installation of Vertical Scrubbers

Gas-liquid separators often encounter the challenge of liquid carry-over, where small liquid droplets become entrained in the produced gas stream. This phenomenon can lead to foaming and reduced capacity in downstream absorption processes, as observed in Iraq’s Khor Mor gas-condensate processing pla...

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Bibliographic Details
Published in:Petroleum chemistry Vol. 64; no. 1; pp. 62 - 74
Main Authors: Sulaiman, Fenk A., Sidiq, Hiwa, Ali, Aryan A., Mohamad, Mirei
Format: Journal Article
Language:English
Published: Moscow Pleiades Publishing 2024
Springer Nature B.V
Subjects:
Chemistry
Chemistry and Materials Science
Design standards
Droplets
Efficiency
Empirical analysis
Foaming
Gas streams
Industrial Chemistry/Chemical Engineering
Inlet flow
Scrubbers
Separation
Separators
Size distribution
Vapor phases
Vessels
phase separation
vertical scrubber
liquid carry-over and droplet size distribution
separation efficiency
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Summary:Gas-liquid separators often encounter the challenge of liquid carry-over, where small liquid droplets become entrained in the produced gas stream. This phenomenon can lead to foaming and reduced capacity in downstream absorption processes, as observed in Iraq’s Khor Mor gas-condensate processing plant. To assess whether liquid carry-over contributes to the foaming issue in the sweetening tower, this study analyzed the liquid droplet size distribution in the gas phase and the gas/liquid separation efficiency of the upstream Alpha, Bravo #1, Bravo #2, and Charlee separators feeding the tower. The analysis was conducted by using the industry-standard process software, Horizontal Vessel and ProSeparator correlations within Aspen HYSYS v.14. The study revealed that Alpha, Bravo #1, and Bravo #2 separators were unable to eliminate all liquid droplets within the specified size, failing to achieve the required efficiency. In response, the study proposes a vertical scrubber design with a standard mesh mist extractor, applying the Arnold–Stewart semi-empirical procedure. The design demonstrated a gas/liquid separation efficiency of 99% under current and future conditions. These findings suggest that the proposed design can serve as an optimal solution to control liquid carry-over, maintain high gas/liquid separation efficiency, and prevent foaming, even with an increase in the vessel inlet flow rate over time.
ISSN:0965-5441
1555-6239
DOI:10.1134/S0965544124020178