Using a Liquefied Gas as a Centrifuge Aid

Patent metadata

Field	Value
Publication number	US-2019106953-A1
Application number	US-201715774075-A
Country	US
Kind code	A1
Filing date	Oct 9, 2017
Priority date	Oct 9, 2017
Publication date	Apr 11, 2019
Grant date	—

Abstract

Extracting and separating solid particulates from a drilling fluid includes combining a stream of drilling fluid containing solid particulates with a liquefied gas to form a mixture having a reduced viscosity and/or density. The mixture enters a centrifugal separator at a pressure sufficient to keep the liquefied gas in a liquid phase where rotational forces promote the separation of at least a portion of the solid particulates from the mixture. At least a portion of the solid particulates are removed to form a fluid stream having reduced solids content. In embodiments the liquefied gas can be selected from the group consisting of an inert gas, an alkane gas, an alkene gas, an alkyne gas, a noble gas, and combinations thereof. The liquefied gas can be removed from the fluid stream after the centrifugal separator and recycled back to be mixed with the stream of drilling fluid containing solid particulates.

First claim

What is claimed is:

1 . A method of extracting and separating solid particulates from a drilling fluid composition comprising:
contacting a first drilling fluid containing solid particulates with a liquefied gas to form a second drilling fluid exhibiting one or more properties that are reduced compared to the same property exhibiting by the first drilling fluid, wherein the one or more properties are selected from viscosity, density, and combinations thereof; introducing the second drilling fluid into a first centrifugal separator, wherein the first centrifugal separator is operated at a first pressure sufficient to maintain liquefied gas present in the second drilling fluid in a liquid phase; rotating the first centrifugal separator to promote separation of at least a portion of the solid particulates from the second drilling fluid; and removing at least a portion of the solid particulates from the second drilling fluid to form a third drilling fluid having reduced solids content compared to the second stream.

2 . The method of claim 1 , wherein the liquefied gas is in either a supercritical or liquid phase while in the second drilling fluid.

3 . The method of claim 1 , wherein the liquefied gas is selected from the group consisting of an inert gas, an alkane gas, an alkene gas, an alkyne gas, a noble gas, and combinations thereof.

4 . The method of claim 1 , further comprising removing the liquefied gas from the third drilling fluid to form a degassed drilling fluid having reduced solids content as compared to the first drilling fluid.

5 . The method of claim 4 , further comprising vaporizing the liquefied gas present in the third drilling fluid to form vaporized gas and separating the vaporized gas from the remaining components present in the third drilling fluid.

6 . The method of claim 5 , further comprising re-liquefying the vaporized gas to form liquefied gas for contact with the first drilling fluid.

7 . The method of claim 1 , further comprising a second centrifugal separator in series with and located after the first centrifugal separator, wherein the first centrifugal separator removes a first group of solids to form the third drilling fluid, the second centrifugal separator removes a second group of solids to form a fourth drilling fluid, and at least a portion of the first group of solids is mixed back into the fourth drilling fluid to form a fifth drilling fluid.

8 . The method of claim 7 , wherein the first centrifugal separator is a centrifuge that removes barite from the drilling fluid prior to the second centrifugal separator that removes undesirable solid particulates.

9 . The method of claim 8 , further comprising removing the liquefied gas from the drilling fluid after the second centrifugal separator to form a degassed drilling fluid having reduced solids content as compared to the first stream of drilling fluid.

10 . The method of claim 9 , further comprising recycling the liquefied gas removed after the second centrifugal separator to be mixed with the first drilling fluid.

11 . The method of claim 9 , further comprising recycling the liquefied gas removed after the second centrifugal separator to be mixed with the third drilling fluid after the removal of the first group of solids and prior to the second centrifugal separator.

12 . The method of claim 7 , wherein liquefied gas is mixed with the drilling fluid streams prior to both the first centrifugal separator and the second centrifugal separator.

13 . The method of claim 7 , further comprising: extracting residual gas and oil from the second group of solids.

14 . The method of claim 13 , further comprising: separating the residual gas from the residual oil, combining the residual gas with the liquefied gas, and combining the residual oil with the degassed drilling fluid.

15 . A method of extracting and separating solid particulates from a drilling fluid composition comprising:
combining a first drilling fluid containing solid particulates with a liquefied gas in either a supercritical or liquid phase to form a second drilling fluid exhibiting one or more properties that are reduced compared to the same property exhibiting by the first drilling fluid, wherein the one or more properties are selected from viscosity, density, and combinations thereof; introducing the second drilling fluid into a centrifugal separator, wherein the centrifugal separator is operated at a pressure sufficient to maintain liquefied gas present in the second drilling fluid in a liquid phase; rotating the centrifugal separator to promote separation of at least a portion of the solid particulates from the second drilling fluid; removing at least a portion of the solid particulates from the second drilling fluid to form a third drilling fluid having reduced solids content compared to the first drilling fluid; vaporizing the liquefied gas and separating the vaporized gas from the third drilling fluid to form a degassed drilling fluid; re-liquefying the vaporized gas to form liquefied gas to be combined with the first drilling fluid.

16 . The method of claim 15 , wherein the liquefied gas is selected from the group consisting of an inert gas, an alkane gas, an alkene gas, an alkyne gas, a noble gas, and combinations thereof.

17 . The method of claim 15 , wherein the centrifugal separator comprises a first centrifugal separator and a second centrifugal separator in series, wherein the first centrifugal separator removes a first group of solids, the second centrifugal separator removes a second group of solids, and at least a portion of the first group of solids is mixed back into the drilling fluid after the removal of the second group of solids.

18 . The method of claim 17 , wherein the first centrifugal separator and second centrifugal separator in series both operate at conditions to maintain the liquefied gas in a liquid or supercritical phase.

19 . A method of extracting and separating solid particulates from a drilling fluid composition using multiple centrifugal separators, the method comprising:
combining a first drilling fluid containing solid particulates with a liquefied gas selected from the group consisting of an inert gas, an alkane gas, an alkene gas, an alkyne gas, a noble gas, and combinations thereof, to form a second drilling fluid exhibiting one or more properties that are reduced compared to the same property exhibiting by the first drilling fluid, wherein the one or more properties are selected from viscosity, density, and combinations thereof; introducing the second drilling fluid into a first centrifugal separator, wherein the first centrifugal separator is operated at a pressure sufficient to maintain the liquefied gas present in the second drilling fluid in a liquid phase; rotating the first centrifugal separator to promote separation of at least a portion of the solid particulates from the second drilling fluid; removing at least a portion of the solid particulates from the second drilling fluid to form a third drilling fluid having reduced solids content compared to the first drilling fluid; introducing the third drilling fluid into a second centrifugal separator, wherein the second centrifugal separator is operated at a pressure sufficient to maintain the liquefied gas present in the third drilling fluid in a liquid phase; rotating the second centrifugal separator to promote the separation of at least a portion of the solid particulates from the third drilling fluid; separating at least a portion of the solid particulates

Assignees

• Halliburton Energy Services Inc

Inventors

• Kleinguetl Kevin G
• Jamison Dale E

Classifications

• E21B21/066

  with further treatment of the solids, e.g. for disposal · CPC title

• B01D21/267

  by using a cyclone · CPC title

• E21B21/065 Primary

  Separating solids from drilling fluids · CPC title

• B01D21/262

  by using a centrifuge · CPC title

• B04B1/20

  discharging solid particles from the bowl by a conveying screw coaxial with the bowl axis and rotating relatively to the bowl · CPC title