Spherical separation device and method for separation

Patent metadata

Field	Value
Publication number	US-10814252-B2
Application number	US-201214346558-A
Country	US
Kind code	B2
Filing date	Aug 13, 2012
Priority date	Sep 23, 2011
Publication date	Oct 27, 2020
Grant date	Oct 27, 2020

Abstract

The present invention relates to an apparatus for separation of high volume flows of mixtures provided with at least two immiscible phases, especially for the first separation steps of flows of water/oil/gas/sand mixture that enter the apparatus as a wellstream mixture. The invention also relates to a method for separation of high volume flows of mixtures provided with at least immiscible phases.

First claim

The invention claimed is:

1. A separation apparatus for separation of volume flows of mixtures provided with at least two immiscible phases, comprising:
a vessel provided with:
an inlet for the mixture provided with the at least two immiscible phases;
a separation interior;
at least one heavy phase outlet for a separated heavy phase fraction located on a lower side of the vessel and being connected with a first subsequent separator located outside of the vessel and downstream of the heavy phase outlet, wherein the separated heavy phase fraction leaving the separator through the heavy phase outlet is fed to the first subsequent separator;
a light phase outlet for a separated light phase fraction located above the heavy phase outlet and being connected with a second subsequent separator located outside of the vessel and downstream of the light phase outlet, wherein the separated light phase fraction leaving the vessel through the light phase outlet is fed to the second subsequent separator;

wherein the vessel comprises at least one substantially spherical shaped casing to be designed for use under a higher external pressure than 1 atmosphere, and
wherein at least one of the first or second subsequent separators is a compact separator,
wherein the compact separator is selected from the group consisting of: centrifugal separators, cyclone separators, coalescers and vortex separators, and
wherein in the separation interior of the vessel a vane diffuser comprising a plurality of vanes is connected to the inlet for enabling separation of the mixture.

2. The separation apparatus according to claim 1 , wherein at the lower side of the vessel a solid particle outlet is provided.

3. The separation apparatus according to claim 1 , wherein the apparatus is designed for use wherein the external pressure is higher than the internal pressure.

4. The separation apparatus according to claim 1 , wherein the vessel comprises plural interconnected spherical shaped casings.

5. The separation apparatus according to claim 4 , wherein the vessel comprises at least two stacked and interconnected spherical shaped casings.

6. The separation apparatus of claim 1 , wherein the second separator contains a light phase outlet and a heavy phase outlet, where the heavy phase out of the second separator does not feed into the vessel.

7. The separation apparatus according to claim 1 , wherein both the first and second subsequent separators are compact separators, wherein the compact separators are individually selected from the group consisting of: centrifugal separators, cyclone separators, coalescers and vortex separators.

8. The separation apparatus according to claim 1 , wherein the separation apparatus is submerged underwater.

9. The separation apparatus according to claim 7 , wherein the separation apparatus is located at the seabed.

10. A method for separation of volume flows of a wellstream mixture provided with at least two immiscible phases comprising the steps of:
A) feeding a volume flow of the wellstream mixture to a vessel provided with at least one substantially spherical shaped casing and a separation interior having a vane diffuser connected to an inlet for enabling separation of the well stream mixture;
B) pre-separating the wellstream mixture in the vessel;
C) feeding a separated heavy phase fraction leaving the vessel to a first subsequent separator,
D) feeding a separated light phase fraction leaving the vessel to a second subsequent separator,
E) subsequent separation of the separated heavy phase fraction and the separated light phase fraction in the respective first and second subsequent separators,
wherein at least one of the first or second subsequent separators is a compact separator selected from the group consisting of: centrifugal separators, cyclone separators, coalescers and vortex separators,
wherein the method is performed in the apparatus of claim 1 .

11. The separation method according to claim 10 , wherein the subsequent separation processes of the separated heavy phase fraction and the separated light phase fraction both take place by through flow of the fractions through the subsequent separators.

12. The separation method according to claim 10 , wherein the wellstream mixture is pre-separated in the vessel according step B) providing two different pre-separated wellstream fractions.

13. The separation method according to claim 10 , wherein the separated light phase fraction leaving the vessel contains less than 40 volume % of liquid.

14. The separation method according to claim 13 , wherein the separated light phase fraction leaving the vessel contains less than 30 volume % of liquid.

15. The separation method according to claim 14 , wherein the separated light phase fraction leaving the vessel contains less than 20 volume % of liquid.

16. The separation method according to claim 10 , wherein the separation apparatus is submerged underwater.

17. The separation method according to claim 16 , wherein the separation apparatus is located at the seabed.

18. A separation apparatus for separation of volume flows of mixtures provided with at least two immiscible phases, comprising:
a vessel provided with:
an inlet for the mixture provided with the at least two immiscible phases;
a separation interior;
at least one heavy phase outlet for a separated heavy phase fraction located on a lower side of the vessel and being connected with a first subsequent separator located outside of the vessel and downstream of the heavy phase outlet, wherein the separated heavy phase fraction leaving the separator through the heavy phase outlet is fed to the first subsequent separator;
a light phase outlet for a separated light phase fraction located above the heavy phase outlet and being connected with a second subsequent separator located outside of the vessel and downstream of the light phase outlet, wherein the separated light phase fraction leaving the vessel through the light phase outlet is fed to the second subsequent separator;

wherein the vessel comprises at least one substantially spherical shaped casing to be designed for use under a higher external pressure than 1 atmosphere, and
wherein at least one of the first or second subsequent separators is a compact separator,
wherein the compact separator is selected from the group consisting of: centrifugal separators, cyclone separators, coalescers and vortex separators,
wherein in the separation interior of the vessel a vane diffuser comprising a plurality of vanes is connected to the inlet for enabling separation of the mixture, and
wherein both the first and second subsequent separators are compact separators, wherein the compact separators are individually selected from the group consisting of: centrifugal separators, cyclone separators, coalescers and vortex separators.

Assignees

• Larnholm Per Reidar
• Lammers Frederik Albert
• Sulzer Management Ag

Inventors

• Larnholm Per-Reidar
• Lammers Frederik Albert

Classifications

• B01D21/2494 Primary

  provided with means for the removal of gas, e.g. noxious gas, air · CPC title

• B01D21/10

  Settling tanks with multiple outlets for the separated liquids · CPC title

• B01D21/0042

  Baffles or guide plates · CPC title

• B01D19/0042 Primary

  modifying the liquid flow (B01D19/0021 takes precedence) · CPC title

• E21B43/34

  Arrangements for separating materials produced by the well · CPC title