Viscous fluid dilution system and method thereof

Patent metadata

Field	Value
Publication number	US-10124307-B2
Application number	US-201615248565-A
Country	US
Kind code	B2
Filing date	Aug 26, 2016
Priority date	Jun 6, 2013
Publication date	Nov 13, 2018
Grant date	Nov 13, 2018

Abstract

A dilution system for a hydraulic fracturing fluid includes a dilution manifold, a hydration unit configured to provide a source of liquid, a diluent line connecting the hydration unit to the dilution manifold, a diluent flow control valve on the diluent line, a hydration tank configured to hydrate a mixed additive, a gravity-driven viscous fluid line connecting an exit of the hydration tank to the dilution manifold, a viscous fluid flow meter on the viscous fluid line, and a viscous fluid control valve on the viscous fluid line.

First claim

What is claimed is:

1. A dilution system for a hydraulic fracturing fluid, the dilution system comprising:
a dilution manifold;
a hydration unit configured to provide a source of liquid;
a diluent line connecting the hydration unit to the dilution manifold, and the diluent line from the hydration unit to the dilution manifold is gravity-driven and pumpless;
a diluent flow control valve on the diluent line;
a hydration tank configured to hydrate a mixed additive;
a gravity-driven viscous fluid line connecting an exit of the hydration tank to the dilution manifold;
a viscous fluid flow meter on the viscous fluid line; and,
a viscous fluid control valve on the viscous fluid line.

2. The dilution system of claim 1 , wherein the dilution system is configured to process shear sensitive polymers including polyacrylamides, copolymers of acrylamides, and terpolymers of acrylamides.

3. The dilution system of claim 1 , wherein the viscous fluid line is pumpless from the hydration tank to the dilution manifold.

4. The dilution system of claim 1 , wherein a ratio of diluent to viscous fluid delivered to the dilution manifold is managed by the viscous fluid flow meter, the viscous fluid control valve, and the diluent flow control valve.

5. The dilution system of claim 4 , wherein the diluent line is meterless.

6. The dilution system of claim 1 , further comprising a mixer configured between the hydration unit and the hydration tank, and a hydration line connecting the hydration unit to the mixer, wherein the hydration line is separate from the diluent line.

7. The dilution system of claim 6 , wherein the hydration tank is configured to enable a continuous processing of a mixed additive from the mixer, and a hydrated mixed additive is a viscous fluid as it passes through the exit of the hydration tank to the viscous fluid line.

8. The dilution system of claim 6 , further comprising a pump directing the liquid from the hydration unit to the mixer on the hydration line.

9. The dilution system of claim 8 , further comprising a flow meter on the hydration line.

10. The dilution system of claim 1 , wherein the dilution manifold is fluidically connected to a blender header of a proppant blender, and a pump directs diluted viscous fluid from the dilution manifold to the proppant blender.

11. The dilution system of claim 10 , further comprising a blender line flow meter configured to measure flow from the dilution manifold to the proppant blender.

12. The dilution system of claim 10 , further comprising a plurality of valves connecting the dilution manifold to the blender header.

13. The dilution system of claim 1 , wherein the dilution manifold includes a dilution manifold header and a dilution manifold header valve, the dilution manifold header valve configured to separate the diluent line from the viscous fluid line at the dilution manifold header.

14. The dilution system of claim 1 , wherein the diluent line is not connected to the hydration tank.

15. The dilution system of claim 1 , further comprising a mixer configured to direct the mixed additive to an input of the hydration tank through a mixed additive line, wherein the diluent line is not connected to the mixed additive line.

16. The dilution system of claim 1 , wherein the hydration tank is configured to increase a residency time of the mixed additive delivered to the hydration tank at an input of the hydration tank before releasing a viscous fluid at the exit of the hydration tank.

17. The dilution system of claim 1 , wherein the diluent line is meterless.

18. A dilution system for a hydraulic fracturing fluid, the dilution system comprising:
a dilution manifold;
a hydration unit configured to provide a source of liquid;
a diluent line connecting the hydration unit to the dilution manifold, and the diluent line is meterless;
a diluent flow control valve on the diluent line;
a hydration tank configured to hydrate a mixed additive;
a gravity-driven viscous fluid line connecting an exit of the hydration tank to the dilution manifold;
a viscous fluid flow meter on the viscous fluid line;
a viscous fluid control valve on the viscous fluid line; and
a blender line flow meter configured to measure flow from the dilution manifold to a proppant blender;
wherein a ratio of diluent to viscous fluid delivered to the dilution manifold is managed by the viscous fluid flow meter, the viscous fluid control valve, and the diluent flow control valve.

19. A dilution system for a hydraulic fracturing fluid, the dilution system comprising:
a dilution manifold;
a hydration unit configured to provide a source of liquid, the hydration unit includes an input header and a plurality of hydration unit valves configured to connect or disconnect the input header from the source of liquid;
a diluent line connecting the hydration unit to the dilution manifold;
a diluent flow control valve on the diluent line;
a hydration tank configured to hydrate a mixed additive;
a gravity-driven viscous fluid line connecting an exit of the hydration tank to the dilution manifold;
a viscous fluid flow meter on the viscous fluid line; and,
a viscous fluid control valve on the viscous fluid line.

20. The dilution system of claim 19 , wherein the diluent line from the hydration unit to the dilution manifold is gravity-driven and pumpless.

Assignees

• Weinstein Jeremy L
• Lambert Bryan Scott
• Gloria Abel A
• Baker Hughes A Ge Co Llc

Inventors

• Weinstein Jeremy L
• Lambert Bryan Scott
• Gloria Abel A

Classifications

• C09K8/90

  of natural origin, e.g. polysaccharides, cellulose · CPC title

• B01F15/0234

  Operations & Transport · mapped topic

• B01F2215/0081

  Operations & Transport · mapped topic

• E21B41/00

  Equipment or details not covered by groups E21B15/00 - E21B40/00 · CPC title

• B01F15/0261

  Operations & Transport · mapped topic