PROCESS FOR HYDRAULIC FRACTURING WITH pH CONTROL

a hydraulic fracturing and control technology, applied in the direction of fluid removal, survey, borehole/well accessories, etc., can solve the problems of increasing the pumping pressure during the fracturing, and affecting the performance of organic polymer friction reducers such as anioni

Inactive Publication Date: 2013-08-15
THE CHEMOURS CO FC LLC
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

[0024]In the hydraulic fracturing process large volumes of water are used. An advantage of the present invention is that when pH is suitably controlled, at least a portion of the water used for fracturing, which can average about 3000 gallons (11,000 liters) per minute, or more, can be flow back and produced water. Flow back water that is recovered from the fracturing operation and produced water may comprise metal salts including ferrous and ferric metal salts, hydrocarbons, and residual biocide, friction reducer and other additives. In the absence of pH control as set forth herein, the presence of metal salts in the produced water interferes with performance of the friction reducer. In certain regions, such as in the Marcellus Shale region, produced water is characterized as having a high iron content.
[0025]Proppant, which keeps an induced hydraulic fracture open during or following a fracturing treatment, is most commonly sand but can also be any other such particulate material with adequate mechanical properties to withstand closure stresses including, for example, ceramic, glass, and bauxite.
[0026]The fracturing fluid may comprise other components, including, for example, polymers, breaking agents, scale inhibitors, corrosion inhibitors, etc. These other components may be added to the biocide or to the water, or still other options for adding are available.
[0027]The process of this invention comprises providing a fracturing fluid by combining water, proppant, an oxidizing biocide, and a friction reducer. This combining step may be in a single step or multiple steps.
[0028]For example, the water may be treated with the biocide and with other components such as a scale inhibitor and a corrosion inhibitor prior to combining the treated mixture with proppant and the friction reducer. The biocide treated water may be stored, for example for periods of time of about 30 minutes or less prior to combining with friction reducer. The water used may consist of all fresh water, usually from a local stream, pond, or potable water supply, or a mixture of fresh water and produced water. The fresh and produced water may be supplied to treatment manifold in a single stream or in multiple streams.
[0029]“Frac tanks” are often used as a source of water to supply a constant flow of water to the fracturing process. Water may be supplied to a blending / mixing device, such as a ribbon mixer into which friction reducer, proppant and biocide or biocide mixture are added to produce the fracturing fluid.

Problems solved by technology

Problems have been encountered in the performance of organic polymer friction reducers such as anionic polyacrylamide polymers (either hydrolyzed to produce acid functionality or copolymerized with acrylic acid).
It has been theorized that use of oxidizing biocides in combination with these polymers causes the polymers to degrade and therefore increasing pumping pressure is necessary during the fracturing operations.
However, many non-oxidizing biocides are not acceptable due to environmental concerns and low efficacy.
At low pH, protonation of the polyacrylamide friction reducers can inhibit its ability to hydrate and unwind rapidly, thus, reducing its friction-reducing ability.
Because of the shortage of fresh water and the cost of treatment and / or disposal of produced water it is desirable to re-use at least a portion of the produced water in subsequent hydraulic fracturing treatments; however, the presence of contaminants, which include oxidizable, acid-producing metal ions, such as soluble Fe2+ and Mn2+, also negatively affects performance of the friction reducers.

Method used

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  • PROCESS FOR HYDRAULIC FRACTURING WITH pH CONTROL

Examples

Experimental program
Comparison scheme
Effect test

example 1

[0039]This example provides the results of friction loop tests which demonstrate the effect of pH on friction reduction of various friction reducing polymers.

[0040]Friction loop tests were carried out at Stim-Lab, Inc. located in Duncan, Okla., using a standard apparatus known to those skilled in the art. For each test, approximately 9 gallons of test fluid was circulated at 10 gallons / minute (approx. Reynolds number of 75,000). The friction reduction was calculated from the pressure drop across a precise length of the test loop.

[0041]The water used to prepare the test fluids was a blend of 40% produced water from the Marcellus shale formation and 60% surface water collected from a location in Pennsylvania. The unadjusted pH of the water was 5.8. For tests run at lower pH, the water was acidified with sulfuric acid. In some cases the acidified water was also treated to contain about 10 mg / L residual ClO2. The test temperature was about 24° C. (75° F.).

[0042]For each test, a baseline...

example 2

[0044]This example demonstrates the pH lowering effect of oxidizing biocide in combination with divalent iron.

[0045]Unbuffered deionized water was adjusted to a pH of 6.0-6.2 with 1N NaOH or HCl as needed. Samples 2B and 2C were prepared from this water and 99.5% iron(II) heptahydrate so that the added Fe2+ content was 25 and 50 mg / L, respectively. Sample 2A was a control sample and contained no added iron. To each of samples 2A-2C, 30 mg / L ClO2 was applied, after which the pH and residual ClO2 was measured about 30 minutes later. Results, which were gathered at ambient laboratory temperatures of about 20-22 C, are summarized in the following table.

Fe2+pHpHClO2 mg / LClO2 mg / LSamplemg / Linitialfinalappliedresidual2A06.186.243028.52B256.103.613018.12C506.103.33014.5

[0046]Control sample 2A, without Fe2+, shows no substantial change in pH with addition of ClO2 and substantially no consumption of ClO2 (the applied and residual amount is substantially the same). In contrast, ClO2 addition t...

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Abstract

A process for hydraulic fracturing including the steps of (a) providing a fracturing fluid by combining water, proppant, an oxidizing biocide, and a friction reducer; (b) introducing the fracturing fluid into a well; and (c) controlling the pH of the fracturing fluid to a pH of at least about 4.5.

Description

FIELD OF THE INVENTION[0001]The present invention relates to the stimulation of the production of subterranean hydrocarbon formations or stimulation of fluid injection into subterranean formations in a hydraulic fracturing process. More particularly, the present invention relates to an improved process for hydraulic fracturing in which performance of additives, in particular, friction reducers, is enhanced.BACKGROUND OF THE INVENTION[0002]The production of oil and natural gas from an underground well (subterranean formation) can be stimulated by a technique called hydraulic fracturing in which a fracturing fluid is introduced into an oil or gas well via a conduit, such as tubing or casing, at a flow rate and a pressure to create, reopen and / or extend a fracture into the well, allowing access to the oil or gas within the formation.[0003]The fracturing fluid is typically a water based solution and may comprise components such as suspended proppants (e.g., sand, bauxite); biocides to i...

Claims

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Application Information

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Patent Type & Authority Applications(United States)
IPC IPC(8): E21B43/26E21B47/00
CPCE21B43/26C09K8/62E21B47/00
Inventor TUFANO, THOMAS PETERVORE, ROY DEANEHRHART, RAYMOND
Owner THE CHEMOURS CO FC LLC
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