Continuous extruded solids discharge

Patent metadata

Field	Value
Publication number	US-2020398235-A1
Application number	US-202016856874-A
Country	US
Kind code	A1
Filing date	Apr 23, 2020
Priority date	Jun 21, 2019
Publication date	Dec 24, 2020
Grant date	—

Abstract

A device for processing oil or gas well waste solids, the device including a pressurizing discharge unit having a casing. The casing includes a solids inlet and a water inlet. The solids inlet receives treated solids into a front end of the casing, where the treated solids are exposed to a reduced pressure in an internal chamber of the casing of less than atmospheric pressure. The water inlet receives water and adds the water to the treated solids in the internal chamber. The casing includes an extruder screw unit, the extruder screw unit having progressive screw sections located inside the internal chamber and corresponding to conveying mixing and pressurizing screw sections. The conveying screw section conveys the treated solids along a long axis length of the extruder screw unit from the solids inlet towards a discharge end of the casing while the reduced pressure is maintained, the mixing screw section mixes the treated solids and the water together to form a paste, and the pressurizing screw section conveys the paste towards the discharge end and generates, in a portion of the casing downstream from the mixing screw section, a backpressure that is greater than atmospheric pressure. The casing includes a die assembly to extrude the paste through an orifice of the die assembly located at the discharge end while maintaining the backpressure on the paste in the internal chamber. Method and system embodiments for processing oil or gas well waste solids are also disclosed.

First claim

What is claimed is:

1 . A device for processing oil or gas well waste solids, the device comprising:
a pressurizing discharge unit having a casing, the casing including: a solids inlet configured to receive treated solids into a front end of the casing, wherein the treated solids are exposed to a reduced pressure in an internal chamber of the casing of less than atmospheric pressure; a water inlet configured to receive water and add the water to the treated solids in the internal chamber; an extruder screw unit, the extruder screw unit having progressive screw sections located inside the internal chamber and corresponding to:
a conveying screw section configured to convey the treated solids along a long axis length of the extruder screw unit from the solids inlet towards a discharge end of the casing while the reduced pressure is maintained,
a mixing screw section configured to mix the treated solids and the water together to form a paste, and
a pressurizing screw section configured to convey the paste towards the discharge end and to generate, in a portion of the casing downstream from the mixing screw section, a backpressure that is greater than atmospheric pressure; and
a die assembly configured to extrude the paste through an orifice of the die assembly located at the discharge end while maintaining the backpressure on the paste in the internal chamber.

2 . The device of claim 1 , wherein, the conveying screw section has a pitch length that is longer than a pitch length of the mixing screw section and longer than a pitch length of the pressurizing screw section, and, the pitch length of the pressurizing screw section is longer than the pitch length of the mixing screw section.

3 . The device of claim 1 , wherein, the conveying screw section has a flight depth that is deeper than a flight depth of the mixing screw section and that is deeper than a flight depth of the pressurizing screw section, and, the flight depth of the mixing screw section is deeper than the flight depth of the pressurizing screw section.

4 . The device of claim 1 , wherein, the conveying screw section has a flight width that is narrower than a flight width of the mixing screw section and narrower than a flight width of the pressurizing screw section.

5 . The device of claim 1 , wherein, the conveying screw section has a helical angle of flight that is greater than a helical angle of flight of the pressurizing screw section.

6 . The device of claim 1 , wherein each of the conveying screw section, the mixing screw section, and the pressurizing screw section have a constant pitch length, flight depth, flight width and helical angle throughout an internal length of the each of the respective sections.

7 . The device of claim 1 , wherein:
the conveying screw section has an internal length that is in a range from about 50 to 75 percent of a total length of the screw unit in the chamber, the mixing screw section has an internal length that is in a range from about 12 to 50 percent of the total length, and the pressurizing screw section has an internal length that is in a range from about 12 to 50 percent of the total length.

8 . The device of claim 1 , wherein the extruder screw unit includes a single continuous screw having the conveying screw section, the mixing screw section, and the pressurizing screw section.

9 . The device of claim 1 , wherein the extruder screw unit includes two or more continuous screws each having parallel internal lengths of the conveying screw section, the mixing screw section, and the pressurizing screw section.

10 . The device of claim 9 , wherein at least portions of the two or more continuous screws are intermeshed with each other.

11 . The device of claim 10 , wherein the conveying screw sections of the two or more continuous screws are intermeshed with each other, the mixing screw sections are not intermeshed with each other and the pressurizing screw sections are intermeshed with each other.

12 . The device of claim 1 , wherein a cross-sectional area of the internal chamber located in the portion of the casing downstream from the mixing screw section is greater than a cross-sectional area of the orifice.

13 . The device of claim 12 , wherein a ratio of the cross-sectional area of the internal chamber located in the portion of the casing downstream from the mixing screw section to the cross-sectional area of the orifice is a value in a range from about 2:1 to 10:1.

14 . The device of claim 1 , wherein a cross-sectional area of the orifice is adjustable.

15 . The device of claim 1 , wherein the die assembly includes a spring loaded die plate or pneumatic valve configured to provide a flow resistance to generate the backpressure.

16 . The device of claim 1 , wherein the casing includes cooling fins, or a cooling coil configured circulate a cooling fluid there-through, to thereby reduce the internal chamber temperature to a temperature that prevents steam generation inside the internal chamber.

17 . The device of claim 1 , the casing further includes a steam outlet, the steam outlet located between the solids inlet and the water inlet, the steam outlet connected to an eductor, the eductor configured to condense steam exiting the steam outlet.

18 . The device of claim 1 , further including a drive module, the drive module including a motor and gearbox coupled to the extruder screw unit, the motor configured to rotate screws of the screw unit and the gear box configured to adjust a rotational speed and rotational direction of the screws.

19 . A method for processing oil or gas well waste solids, the method comprising:
receiving treated solids into a solids inlet, the solids inlet located in a front end of a casing of a pressurizing discharge unit, wherein the treated solids are exposed to a reduced pressure in an internal chamber of the casing of less than atmospheric pressure; adding water to the treated solids in the internal chamber through a water inlet located in the casing; rotating an extruder screw unit located in the internal chamber, the extruder screw unit having progressive screw sections corresponding to a conveying screw section, a mixing screw section and a pressurizing screw section, including:
conveying, by the conveying screw section, the treated solids along a long axis length of the extruder screw unit, from the solids inlet towards a discharge end of the casing while the reduced pressure is maintained,
mixing, by the mixing screw section, the treated solids and the water together, to form a paste, and
conveying, by the pressurizing screw section, the paste towards the discharge end, and generating, in a portion of the casing downstream from the mixing screw section, a backpressure that is greater than atmospheric pressure; and
extruding the paste through an orifice of a die assembly located at the discharge end while maintaining the greater than atmospheric backpressure on the paste in the internal chamber.

20 . An oil or gas well drilling system, the system comprising:
a feed line configured to transport waste solids to a thermal extraction unit, the thermal extraction unit configured to extract hydrocarbon and water vapor from the waste solids to form treated solids, wherein the treated solids are maintained at a reduced pressure of less than atmospheric pressure; a flow conduit connected to transport the treated solids to a pressurizing discharge unit while maintaining the reduced pressure, wherein: the pressurizing discharge unit has a casi

Assignees

• Halliburton Energy Services Inc

Inventors

• Kapila Rajesh C
• Hoffman Barry

Classifications

• B09B3/32

  Compressing or compacting · CPC title

• B09B3/80

  involving an extraction step · CPC title

• B09B3/40

  involving thermal treatment, e.g. evaporation (processes using mineral binders involving a melting or softening step B09B3/29; involving radiation B09B3/50) · CPC title

• B09B3/38

  Stirring or kneading · CPC title

• E21B21/06

  Arrangements for treating drilling fluids outside the borehole · CPC title