IP Library Granted Patent US 11,084,975
Granted Patent B1
US 11,084,975 · App. 16/566,743 · Granted Aug 10, 2021

Process for using subterranean produced fluids for hydraulic fracturing with cross-linked gels while providing elimination or reduction of formation clay stabilizer chemicals

Inventors: Mark Patton (Valinda, CA); Jinxuan Hu (Spring, TX); Barry Hinton (Brighton, CO); Ed Keenan (Indio, CA)
Assignee: HYDROZONIX, LLC
C09K8/665B01F3/0861B01F15/0022B01F15/00422C09K8/66C09K8/685C09K8/845C09K8/887E21B21/062G05D11/132B01F2215/0081E21B43/26
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Quick Facts
Patent No.
US 11,084,975
App. No.
16/566,743
Granted
Aug 10, 2021
Kind
B1
Abstract

A system and process for defining, blending and monitoring fresh water with subterranean produced formation fluids, with particular constituents of the blended waters being controlled for proper use in gel-type hydraulic fracturing operations. On-site measurements and calculations of clay stabilization replacement, through a Potassium Chloride (KCl) Equivalency calculation, provide feedback on water constituent adjustments that may be needed just prior to the gel-based hydraulic fracturing process. This assures adequate gel cross-linking times, delayed gel cross-linking times, and clay stabilization in the formation to be fractured.

Claims (12)

1. A system for blending fluids for hydraulic fracturing, comprising:

a blending chamber configured to receive and blend a fresh water input and a produced fluid input into a blended water output; and

a blended water output sample point;

wherein an actual boron concentration for the blended water output is determined from one or more samples obtained at the blended water output sample point; and

further wherein the amount of fresh water input and the amount of produced fluid input are determined based upon a target Potassium Chloride Equivalency value or range for the blended water output.

2. The system of claim 1 , further comprising a fresh water input sample point upstream of the blending chamber.

3. The system of claim 1 , further comprising a produced fluid input sample point upstream of the blending chamber.

4. The system of claim 1 , further wherein the amount of fresh water input and the amount of produced fluid input are determined upon a chloride concentration in the fresh water input and a chloride concentration in the produced fluid input.

5. The system of claim 1 , wherein an actual Potassium Chloride Equivalency value for the blended water output is determined from one or more samples obtained at the blended water output sample point.

6. The system of claim 5 , wherein the amount of the fresh water input and the amount of the produced fluid input are adjusted if the actual Potassium Chloride Equivalency value is not substantially equal to the target Potassium Chloride Equivalency value or within the target Potassium Chloride Equivalency range.

7. The system of claim 1 , wherein the blended water output is produced on a batch basis for a stage in a hydraulic fracturing operation.

8. The system of claim 1 , wherein the blended water output is produced for injection in an injection well.