Patent Application
20170198206
Hydraulic fracturing is a common and well-known enhancement method for stimulating the production of hydrocarbon bearing formations. The process involves injecting fluid down a wellbore at high pressure. The fracturing fluid is typically a mixture of water and proppant. The proppant may be made of natural materials or synthetic materials.
Generally the fracturing process includes pumping the fracturing fluid from the surface through a tubular. The tubular has been prepositioned in the wellbore to access the desired hydrocarbon formation. The tubular has been sealed both above and below the formation to isolate fluid flow either into or out of the desired formation and to prevent unwanted fluid loss. Pressure is then provided from the surface to the desired hydrocarbon formation in order to open a fissure or crack in the hydrocarbon formation.
Typically large amounts of fluid are required in a typical hydraulic fracturing operation. Additionally, chemicals are often added to the fluid along with proppant to aid in proppant transport, friction reduction, wettability, pH control and bacterial control. Typically, the fluid is mixed with the appropriate chemicals and proppant particulates and then pumped down the wellbore and into the cracks or fissures in the hydrocarbon formation.
Due to the large amounts of fluid required in a typical hydraulic fracturing operation as well as the ecological implications many operators would prefer to utilize the water that is locally available. For instance in many regions it may be advantageous to use sea water, produced water, or brine as the base fluid during drilling or fracturing operations.
The base fluids for hydraulic fracturing fluid systems have historically been limited by the concentration of salts, typically sodium chloride. Operators have found that while certain hydraulic fracturing fluids systems may work in the presence of salt the efficacy of such systems diminishes as temperature increases. As pressure increases on the service companies and operators to find alternatives to the use of high quality water sources, such as fresh potable water, as the base fluid for their hydraulic fracturing operations, and as scrutiny is increasing over disposal practices for produced water and flowback, the pressure pumping marketing continues to pursue fracturing fluid additives or systems that will enable the use of water having higher concentrations of salts as the base fluid.
An alternative approach to enabling the use of certain hydraulic fracturing systems in the presence of salt and relatively high temperatures, ie temperatures above 260° F., is to add a polyol to the system. In particular it has been found beneficial to use a polyol such as propylene glycol, methanol, and even sugar alcohols to enhance the viscosity of a cross-linked polymeric viscosifier.
One embodiment is to stabilize the gel system by preventing the hydrolysis of the glycosidic linkage or the oxidative/reductive depolymerization where the free radicals are deviated from scission of the polysaccharide chain to attach the hydroxyl groups of the polyols by stabilizing the system either by scavenging oxygen in the polymers solutions with sodium thiosulfate among others.
The new approach includes adding polyols at concentrations up to 50 gallons per thousand to a cross-linked polymer viscosifier such as guar and derivatives, cellulose and derivatives and acrylamide polymer and copolymers with a zirconate cross-linker in order to improve the rheological profile at temperatures above 260° F. The polyols can include diols like ethylene and propylene glycol, triols like glycerol and other sugar alcohols like arabitol, manitol, sorbitol, xylitol etc.
The description that follows includes exemplary apparatus, methods, techniques, or instruction sequences that embody techniques of the inventive subject matter. However, it is understood that the described embodiments may be practiced without these specific details. Any references to sea water or brine, should be understood to include any salt laden water including sea water, produced water, and brine.
A viscosifying agent may be a cellulosic polymer including, but not limited to, carboxyalkyl cellulose or carboxyalkyl cellulose and may be crosslinked with transition metals like zirconate derivatives, titanate derivatives, and aluminate derivatives and combinations thereof.
Viscosifying agents may be guar and its derivatives including, but not limited to, carboxy alkyl guars, such as carboxy methyl hydroxy propyl guar, hydroxyl propoyl guar, and carboxy methyl guar. Other examples of such guars include, without limitation, xanthan, scleroglucan and Welan gums. Such viscosifiers may be crosslinked with borates, borate related crosslinkers, transition metals like zirconate derivatives, aluminate derivatives, and combinations thereof.
Viscosifying agents may be synthetic viscosifiers including, but not limited to, acrylic and acrylamide polymers and copolymers, polyvinyl alcohols, ester and polyether. Such viscosifiers may be crosslinked with borates, borates related crosslinkers, transition metals like zirconate derivatives, aluminate derivatives, and combinations thereof.
Viscosifying agents such as sulfonated gelling agents which may be any sulfonated synthetic polymers including, but not necessarily limited to sulfonated polyvinyl alcohol, sulfonated polyacrylate, sulfonated polyacrylamide, sulfonated galactomannan gums, sulfonated cellulose, acrylic acid copolymers or any combination thereof may be used.
A suitable crosslinking agent may be used with the viscosifiers where the crosslinking agent may be any compound that increases the viscosity of the fluid by chemical crosslinking, physical crosslinking, or any other mechanisms. For example, the gellation of a hydratable polymer can be achieved by crosslinking the polymer with metal ions including boron, zirconium, and titanium containing compounds, or mixtures thereof. One class of suitable crosslinking agents are organotitanates. Another class of suitable crosslinking agents are borates. Suitable crosslinking agents include, but are not limited to, zirconium triethanolamine complexes, zirconium acetylacetonate, zirconium lactate, zirconium carbonate, and chelants of organic alpha hydroxyl corboxylic acid and zirconium.
In addition to the embodiments described above, the hydraulic fracturing fluid additives described above may also be included in the treatment chemistry. This list of additives is not exhaustive and additional additives known to those skilled in the art that are not specifically cited below fall within the scope of the invention
While the embodiments are described with reference to various implementations and exploitations, it will be understood that these embodiments are illustrative and that the scope of the inventive subject matter is not limited to them. Many variations, modifications, additions and improvements are possible.
Plural instances may be provided for components, operations or structures described herein as a single instance. In general, structures and functionality presented as separate components in the exemplary configurations may be implemented as a combined structure or component. Similarly, structures and functionality presented as a single component may be implemented as separate components. These and other variations, modifications, additions, and improvements may fall within the scope of the inventive subject matter.
