Method for extending turndown in a gas-liquid separator

Patent metadata

Field	Value
Publication number	US-9248392-B2
Application number	US-201213718597-A
Country	US
Kind code	B2
Filing date	Dec 18, 2012
Priority date	Dec 18, 2012
Publication date	Feb 2, 2016
Grant date	Feb 2, 2016

Abstract

A system and process for extending turndown in a gas-liquid separator is presented. The system includes a first mist extractor with a first operating range and a second mist extractor with a second operating range. The mist extractors are generally of the same type, with the second operating range being different than the first operating range. A gas stream containing entrained liquid droplets flows through the first mist extractor and then through the second mist extractor. Each mist extractor coalesces and captures the liquid droplets within its own operating range, expanding the overall operating range of the separator. Additional mist extractors may be added to cover any gap between the first and second operating ranges.

First claim

What is claimed is:

1. A process for extending turndown in a gas-liquid separator, the process comprising the steps of:
flowing a gas stream with entrained liquid droplets through a first and a second mist extractor located in a gas-phase area of the gas-liquid separator and arranged in series with one another, said mist extractors being a same kind of mist extractor but having a different cross-sectional area A 1 and A 2 , respectively, the cross-sectional area A 2 of the second mist extractor being sized according to an equation A 2 =K 1 A 1 T 2 /K 2 T O where:
K 1 is a design upper limit K-factor of the first mist extractor,
K 2 is a design upper limit K-factor of the second mist extractor,
T 2 is a targeted turndown of the second mist extractor, and
T O is a targeted turndown of the gas-liquid separator, T O ≠T 2 .

2. A process according to claim 1 wherein the gas stream from the second mist extractor exits the separator through a gas outlet.

3. A process according to claim 1 wherein an operating range of the second extractor is lower than an operating range of the first mist extractor.

4. A process according to claim 1 wherein the cross-sectional area A 2 of the second mist extractor is greater than K 1 A 1 / K 2 T 1 where T 1 is a targeted turndown of the first mist extractor, T a ≠T 2 .

5. A process according to claim 1 further comprising the step of flowing the gas stream with entrained liquid droplets through a third mist extractor located in the gas-phase area of the gas-liquid separator and arranged in series with the first and second mist extractors, the third mist extractor being a same kind of mist extractor as the first and second mist extractors, the cross-sectional area A 2 of the second mist extractor being greater than K 1 A 1 / K 2 T 1 where T 1 is a targeted turndown of the first mist extractor.

6. A process according to claim 1 wherein the targeted turndown T 2 of the second mist extractor is a turndown for a flow rate below a designed minimum operating flow rate of the gas-liquid separator.

Assignees

• Cameron Int Corp

Inventors

• Brown Michael R

Classifications

• B01D45/08

  by impingement against baffle separators · CPC title

• B01D45/16 Primary

  generated by the winding course of the gas stream {, the centrifugal forces being generated solely or partly by mechanical means, e.g. fixed swirl vanes} · CPC title

• B01D45/00 Primary

  Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces · CPC title

• B01D1/305 Primary

  Demister (vapour-liquid separation) · CPC title

• B01D46/003

  including coalescing means for the separation of liquid · CPC title