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Methods, systems and compositions for controlled linking of water solutions for bore hole processing |
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IPC classes for russian patent Methods, systems and compositions for controlled linking of water solutions for bore hole processing (RU 2515109):
Production of granulate from foam glass, granulate of foam glass and its application / 2514070
This invention relates to production of foam glass granulate. Proposed method comprises preparation of initial components of the mix including 80-95% of glass and 5-20% of liquid glass hydrate with a portion of crystallisation water in amount of 1-2 wt % of solid substance. Note here that said liquid glass hydrate makes a sole foaming agent. Glass is ground and initial materials are mixed, then pelletised to get green granulate. Said green granulate is mixed with separation agent taken in amount of 10-40% of the mix. The latter comprises green granulate and separation agent. Said mix is heated to processing temperature. Said temperature is as high as glass minimum sintering temperature decreased by liquid glass hydrate and smaller than glass fusion temperature. This allows, at primary stage, to close pores on green granulate grain surface and, at second stage, to release crystallisation water from said liquid glass hydrate to cause its thermal expansion. This makes green granulate grains swell to make granulate from foam glass. Now, granulate is cooled down.
Method of magnesian-quartz proppant production / 2514037
Invention relates to production of ceramic magnesian-quartz proppant intended for use as propping substances in oil or gas production by hydro fracturing. Proposed method comprises making of ceramic slurry, adding the water-soluble binder thereto, drop formation by bringing vibratory effects on laminar jet by the main frequency, solidification of drops in fixing agent in water solution and annealing. Note here that in the case of changing of slurry laminar jet rheological properties, additional vibratory effects are brought thereon at frequency pother than said main one.
Method for consolidation of liquid stages in fluid system for injection into well / 2513568
Invention relates to consolidation of liquid stages and can be applied to fluid system used for injection into a well. Method for consolidation maintenance of liquid stages in the fluid system used for injection into a well containing an interfacial fluid of another origin adjoining to the liquid stage lies in mixing of solid particles to at least liquid stage or to adjoining interfacial fluid in quantity when discrete borders of the interfacial fluid are formed between the stage and adjoining interfacial fluid and further injection of fluid system into the well bore. Method for consolidation maintenance of liquid stages in the fluid system used for injection into the well containing an interfacial fluid of another origin adjoining to the liquid stage lies in mixing of solid particles to at least liquid stage or to adjoining interfacial fluid in quantity when in streamline conditions discrete borders of the interfacial fluid are formed between the stage and adjoining interfacial fluid and at least a part of solid particles have adhesion properties promoting aggregation of solid particles at least inside the liquid stage or adjoining interfacial fluid and further injection of fluid system into the well bore.
Carbonate formation hydraulic fracturing method / 2509883
In a carbonate formation hydraulic fracturing method involving perforation of well walls at the required interval of the well with channels with depth of not less than length of a stress concentration zone in rocks from the well shaft, lowering to the well of the tubing string with a packer, sealing of the tubular annulus with the packer above the perforation interval, performance of hydraulic formation fracturing by stage pumping to the well of gel-like fracturing liquid and acid, hydraulic fracturing of carbonate formation is performed in series at several stages; with that, at the fist stage, gel-like fracturing liquid is pumped in the volume of at least 6 m3; at the second stage, gel-like fracturing liquid mixed with a propping agent is pumped. As the propping agent, metallic spheres with particle size of 12/18, or 16/20, or 20/40 mesh, which are made from magnesium metal, are used. The propping agent is pumped in portions with subsequent increase in its concentration mixed with gel-like fracturing liquid; at the third stage, forcing-through liquid - service water is pumped in the volume equal to inner volume of the tubing string lowered to the well; at the fourth stage, chlorhydric acid is pumped in the volume of at least 0.6-0.7 of total volume of gel-like fracturing liquid; at the fifth stage, forcing-through liquid - service water is pumped in the volume equal to the volume of the tubing string lowered to the well plus 0.2 m3.
Delayed fracture of structure of fluid media for well treatment / 2509879
Treatment method of an underground formation pierced with a well involves introduction of treating fluid medium to the well; cross-linking of hydrated polymer to increase viscosity of treating fluid medium at least for some of its parts and super cross-linking of cross-linked polymer for delayed fracture of structure of the treating fluid medium. The treatment method of the underground formation pierced with the well involves introduction to the well of the treating fluid medium containing a propping agent suspended in a carrier thickened with cross-linked polysaccharide for deposition of the filler in a fracture, super cross-linking of the cross-linked polymer for fracture of fluid medium and its flowing to the well. The method involves preparation of the treating fluid medium and its introduction to the treated structure, cross-linking of the hydrated polymer to increase viscosity of the treating fluid medium and super cross-linking of the cross-linked polymer for delayed fracture of structure of the treating fluid medium.
Method of pulse hydraulic fracturing implementation / 2507390
Method includes creation of pressure differential between wellbore area and well cavity by means of creation of pressure periodic pulses in wellbore area. Preliminary estimated is time of displacement of fluid mass movement wave from the mouth to specified site of horizontal well and length of extension and healing of formation cracks in horizontal well with two mouths. Filling valve of the first mouth is opened relative to the second mouth with time delay for provision of fluid mass movement waves from both mouths to specified site of wellbore area simultaneously. In horizontal well with one mouth formed are two consequent fluid mass movement waves, time delay between the first and the second waves is chosen based on provision of simultaneous supply of the first and the second fluid mass movement waves repulsed from sump to the specified site of horizontal well.
Method of formation hydraulic fracturing / 2507389
Method includes filling formation with mixture of fracturing liquid with proppant agent. As proppant agent gas crystallohydrates are used. Filling is performed under thermobaric conditions of existence of gas crystallohydrates. After formation fracture gas crystallohydrates are decomposed with extraction of gaseous phase additional to splitting macro and micro-cracks of formation fracture. Filling of fracturing liquid mixture with proppant agent, formation fracture and crystallohydrates decomposition are performed one or several times.
Method of obtaining proppant (versions) and method of hydraulic fracturing of stratum with application of obtained proppant (versions) / 2507178
Invention relates to ceramic proppant and to method of its manufacturing, as well as to method of hydraulic fractioning of stratum. Ceramic proppant includes multiple sintered spherical granules and is manufactured from raw material mixture, which contains first component, selected from aluminium oxide, source of aluminium oxide, second component, which is boron source, and third component, selected from group, consisting of wollastonites, magnesium silicates, olivines, silicon dioxides, silicon carbides, silicon nitrides, as well as compounds of calcium, potassium, sodium, barium, iron, zinc, lithium, ammonium in form of oxides, chlorides, nitrides, nitrites, carbides, carbonates, hydrocarbonates, fluorides, fluorites, sulfates, phosphates, and dolomites, titanium oxides, calcium carbides; and their mixtures, with weight ratio of aluminium oxide/boron oxide in proppant in dry state constituting from approximately 98:30 to approximately 70:2, and apparent density of proppant constitutes 0.2-2.2 g/cm3.
Oil-field biocide made from peracetic acid and method for use thereof / 2506300
Invention relates to biocide compositions for aqueous fluid agents used in oil- and gas-field operations. The biocidal composition of the aqueous fluid medium for treating wells contains a polymer or a copolymer for modifying viscosity of the fluid medium, a monocarboxylic peracid in an antimicrobial amount ranging from about 1 ppm to about 1000 ppm, and hydrogen peroxide in a concentration lower than that of the peracid in an aqueous medium. Said composition, containing a polymer or copolymer, reduces viscosity of the fluid medium, reduces friction or increases viscosity, and the acid is a precursor. The method of providing biocidal activity in the well treatment fluid medium involves adding to the well treatment fluid medium said composition which contains a polymer or copolymer to modify viscosity and feeding said medium into the underground medium. The invention is developed in subclaims.
Addition of non-ionic surfactants to water soluble block copolymers to increase stability of copolymers in aqueous solutions containing salt and/or surfactants / 2506299
Invention relates to extraction of hydrocarbons from underground formations. An aqueous composition containing a mixture of water, about 0.05-10 wt % of the total weight of at least one water-soluble block copolymer, containing: at least one block which is water-soluble by nature, which contains at least 34 wt % hydrophilic links relative the total number of links of the water-soluble block, and containing hydrophobic links and at least one hydrophobic block containing 67 wt % hydrophobic links relative the total number of links of the hydrophobic block, about 0.01-10 wt % of the total weight of a non-ionic surfactant with HLB value ranging from 1 to 12, and about 0.1-20 wt % of the total weight of at least one inorganic salt. The method of extracting hydrocarbons from underground formations involves feeding an aqueous fluid containing said composition into the formation. The method of forming cracks in an underground formation surrounding a well bore involves a step of feeding a fluid containing said composition into the well for hydraulic fracturing.
Control of equivalent circulating density (ecd) at deep water drilling / 2514866
Invention is related to oil well drilling. The method for provision of substantially permanent mud flow characteristics within the temperature range from about 120°F (49°C) up to about 40°F (4°C) includes addition to drilling mud of an additive that contains the product of carboxylic acid reaction having at least two carboxyl fragments and polyamine with at least two functional amine groups provided that the additive does not contain alkoxylated alkylamides and/or amides of fatty acids. The composition consists of the product of carboxylic acid reaction having at least two carboxyl fragments and polyamine with at least two functional amine groups provided that the additive does not contain alkoxylated alkylamides and/or amides of fatty acids. The oil-based drilling mud contains the above composition.
Method for manufacturing of light-weight high-silica magnesium-containing proppant for production of shale hydrocarbons / 2513792
Method includes grinding of preliminary treated feed stock based on natural silica and feldspar sand and serpentine rock, its granulating and sintering; during grinding low-melting red-burning clay is added additionally to the feed stock with the following ratio of components, % by weight: silica and feldspar sand - 70-90, serpentine rock - 5-15, red-burning clay - 5-15, at that the clay is dried preliminary at temperature of 200-400°C and sintering of granules is made at temperature of 1100-1200°C. The invention is well-developed in the subclaim.
Method for consolidation of liquid stages in fluid system for injection into well / 2513568
Invention relates to consolidation of liquid stages and can be applied to fluid system used for injection into a well. Method for consolidation maintenance of liquid stages in the fluid system used for injection into a well containing an interfacial fluid of another origin adjoining to the liquid stage lies in mixing of solid particles to at least liquid stage or to adjoining interfacial fluid in quantity when discrete borders of the interfacial fluid are formed between the stage and adjoining interfacial fluid and further injection of fluid system into the well bore. Method for consolidation maintenance of liquid stages in the fluid system used for injection into the well containing an interfacial fluid of another origin adjoining to the liquid stage lies in mixing of solid particles to at least liquid stage or to adjoining interfacial fluid in quantity when in streamline conditions discrete borders of the interfacial fluid are formed between the stage and adjoining interfacial fluid and at least a part of solid particles have adhesion properties promoting aggregation of solid particles at least inside the liquid stage or adjoining interfacial fluid and further injection of fluid system into the well bore.
Method of producing ceramic proppants / 2513434
Invention refers to oil and gas industry, and namely to the manufacturing procedure of ceramic proppants intended to be used as propping agents at production of oil or gas using the formation hydraulic fracturing method (FHF). According to the manufacturing procedure of ceramic proppants that includes pretreatment of feed stock, milling and formation of granules (granulation), drying and sintering of granules, treatment of their surface with reagent; at milling stage a special water-insoluble sintering agent is added to the feed stock and at granulation stage a cellulating agent containing a water-soluble mineral acid salt is diluted in the granulation liquid; sintering agent and cellulating agent have the following ratio in % in excess of the feed stock weight: cellulating agent - 0.1-1.5, sintering agent - 0.1-2.0, and the above treatment is made by capillary imbibition of the granules porous shell with the solution.
High-penetration grouting mortar / 2513220
Invention relates to oil and gas industry, particularly well repairing and casing, and can be used in remedial cementing for sealing off extraneous water and gas overflow channels in the cement column outside the production casing. The grouting mortar contains, pts.wt per 100 pts.wt microcement CS BTRUO Micro: filtrate reducer PF-BMC 0.25-0.75, setting retarder ZS BMC 0.50-3.00, microsilica MK-85 0.00-10.00, antifoaming agent 0.10-0.30, fresh water 70.0-80.0.
Composition and method for diverting injected fluids to achieve improved hydrocarbon fluid recovery / 2511444
Invention relates to compositions and methods which can be used to improve oil recovery. Disclosed is a composition which contains expandable cross-linked polymeric microparticles having an unexpanded volume average diameter of 0.05-5000 mcm and cross-linking agent content of 100-200000 ppm of hydrolytically labile silyl ester or silyl ether cross-linking agents. Also disclosed is a method of improving recovery of hydrocarbon fluids using said composition.
Method of aluminium powder activation / 2509790
Invention relates to powder metallurgy, particularly, to activation of disperse aluminium powder combustion and can be used in various branches of industry. Proposed method comprises impregnation of initial powder with activator based on vanadium oxide compound. Gel is used as said activator containing 4.0-8.2 g/l of vanadium obtained by melting of vanadium oxide or vanadium oxide and lithium or sodium carbonate or vanadium oxide and boric acid or mix thereof with subsequent addition of the melt to distilled water at intensive mixing and curing. Initial aluminium powder is impregnated with said gel at gel-to-aluminium powder ratio making 2 ml:1 g. Then produced mass is filtered at vacuum filter and dried at 50-60°C for 0.5-1 h.
Foaming aqueous composition / 2509096
Foaming aqueous composition, which contains a foaming agent which contains at least one surfactant, contains triethanolamine oleic acid soap and disubstituted sodium phosphate, with the following ratio of components, wt %: foaming agent 9.0-31.0, triethanolamine oleic acid soap 0.2-6.0, disubstituted sodium phosphate 0.2-2.0, water - the balance.
Method of regenerating hydrate inhibitor / 2508308
Invention relates to a method of producing a lean liquid hydrate inhibitor composition from a rich liquid hydrate inhibitor composition in which the liquid hydrate inhibitor is characterised by a boiling point above that of water. According to the invention, two lean inhibitors are obtained, one free of salt and the other containing salt.
Grouting mortar for cementing horizontal holes / 2508307
Proposed grouting mortar comprises grouting Portland cement PTTS- IG-CC-1, fluid loss reducing agent HYDROTSEM, supersoftener - polyether carboxylate Melflux F or sulphuretted melamine-phenolic resin TSEMPLAST MF, antifoamer POLITSEM DF and setting accelerator, i.e. calcium chloride, and water. It differs from known compositions in that it includes extra mineral additive, i.e. metakaolin or Meta-Mix-1, or CON MIX SF1, or MIKRODUR, at the following ratio of components. Wt %: PTTS IG-CC-1 - 93.35-98.9, HYDROTSEM - 0.1-0.5, said csupersoftener - 0.05-0.3, POLITSEM DF - 0.1-0.3, said mineral additive - 0.5-1.0, calcium chloride - 0.1-2.0, water to water-cement ratio of 0.45-0.55.
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FIELD: chemistry. SUBSTANCE: invention relates to water-based gelling liquids for processing underground formations. Composition for reducing time of linking of water solutions of linked organic polymer includes said polymer, mixed with aqueous basic liquid, borate linking agent, which has solubility in water at 22°C (71.6°F) in the range from 0.01 kg/m3 to 10 kg/m3, and composition of linking modifier in amount, reducing time of linking, which increases rate, at which linking agent provides gelling of linked organic polymer, where composition of modifier contains 90-98% vol. of the first and 2-10% vol. of the second modifiers of linking. Method of underground formation processing includes obtaining liquid for processing, which includes mixing aqueous basic liquid and linked thickening organic polymer, soluble in aqueous basic liquid, hydration of liquid for processing, obtaining borate-based linking composition, which contains borate linking agent, which has solubility, mentioned above; obtaining solution of modifier of linking, which contains 90-98% vol. of the first and 2-10% vol. of the second modifiers of linking; mixing linking composition and solution of modifier of linking; addition of obtained mixed composition to hydrated liquid and delivery of liquid for processing into underground formation. Invention is developed in dependent claims. EFFECT: increased efficiency of control of linking in case of changing pH and in wide interval of temperatures in formation. 21 cl, 10 ex, 13 tbl
Background of invention The scope of the invention The invention described and disclosed in this application, generally relate to compositions and methods for controlling the speed of gel formation in liquids, water-based, used for treatment of underground formations. More specifically, this invention relates to improved compositions used to control gelation or crosslinking of polysaccharides in aqueous solutions with slightly soluble borates, as well as to their application in the allocation of underground hydrocarbons. The level of technology Many underground containing and/or producing hydrocarbon reservoirs require one or more operations of stimulation, such as hydraulic fracturing, to effectively produce hydrocarbons. Borates represented some of the previously used cross-linking agents used to increase the viscosity and the ability to transport rasklinivanie water stimulating liquids based on Guara, they have been successfully used in numerous reservoirs at temperatures from low to moderate (<200°F). However, as the empowerment of detailed exploration of hydrocarbon deposits have been a growing number of underground tanks with temperatures over 200°F and the mouth is owino, what normal used borates and get stitched fluid have inadequate rheological stability. Thus, as the emergence of high-temperature (>200°F) liquids for stimulating wells, attention was drawn to maximize thermal stability, rheological properties of fluids. In particular, we have created cross-linking agents based on titanium and zirconium because of their ability to provide a stable, controlled to some extent binding in the underground environment with high temperatures. Frac fluid, which is stitched using ion titanate, lead zirconate and/or borate (with the use of compounds that generate these ions in the liquid), sometimes contain additives, which are intended to slow the duration of the crosslinking reactions. Such agents, retarding the reaction of crosslinking that allow you to pump fluid down in the underground formation prior to the beginning of the reactions of stitching, thereby enabling to achieve modification and operational flexibility of fracturing fluid. In addition, the use of these additives to control the gelation can be beneficial from the point of view of operation of the injection wells, especially because this application allows you to reduce the amount of pressure required to pump fluids clicks the development wells. This in turn could lead to reduced hardware requirements and reduced the cost of maintaining work-related pumps and uploaders equipment. Examples of previously known agents that slow reaction staple that were documented and entered into the composition of fracturing fluids, water-based, include organic polyols, such as sodium gluconate, glucoheptonate sodium, sorbitol, glyoxal, mannitol, phosphonates and aminocarbonyl acids and their salts (EDTA, DTPA, and so on). Earlier it was reported about a whole range of additional classes of additives and compounds to slow the stitching used to control such deceleration and final viscosity liquids for well treatment, such as frac fluid. You can imagine that the supplements and ways to control gelation differ from each other depending on whether the cross-linking agent is a staple on the basis of borate or staple on the basis of a transition metal (for example, Zr or Ti). In General, the agents used to slow the crosslinking of guar and guar fluids type, are polyfunctional organic compounds, which have chelating ability and can form strong bonds with itself cross-linking agent. Some classes of agents to date have been described, especially supplements d is I controlled fusion using compounds based on zirconium and titanium. For example, in the publication Putzig et al. [SPE Paper No. 105066, 2007] was described hybrid agent to slow down under the trademark TYZOR®(DuPont) to slow the increase in the viscosity of fracturing fluids based on derivatives of guar, made of various conventional suturing based on zirconium and titanium in a wide range of pH and under different conditions. Other agents that cause slowdown for such organic cross-linking agents based on transition metals include hydroxycarbonate acid, such as acid, described in U.S. patent No. 4797216, No. 4861500, Hodge, polygalacturonase acid containing from 3 to 7 carbon atoms, Conway described in U.S. patent No. 4470915 and alkanolamine, such as the agents based on triethanolamine, available under the name TYZOR (E.I. du Pont de Nemours and Co., Inc). However, the application of many of these cross-linking agents based on transition metals and additives, which cause deceleration of the staple, often expensive, sometimes was associated with significant deterioration (often more than 80 %) permeability gaskets propping agent for use in hydraulic fracturing operations, especially in formations with higher temperatures [Penny, G.S., SPE 16900 (1987); Investigation of the Effects of Fracturing Fluids Upon the Conductivity of Proppants, Final Report, (1987) STIM-LAB Inc. Proppant Consortium (1988)]. Was also described several approaches to controlling the fusion process in liquids containing totally the Yu-soluble borate crosslinking agents. For example, it was reported that agents that cause slowdown when using cross-linking agents based on boron, are some polyhydroxylated compounds such as sugar, restored sugars and polyols, such as glycerin. Also described functionalized agents on the basis of aldehydes and dialdehydes for completely soluble borates, such as compounds described in U.S. patent No. 5082579 and 5160643, Dawson. However, many compounds of these agents to control gelation used in compositions with cross-linking agents based on boron, are strongly dependent on pH and temperature, and cannot reliably be used in underground environments with elevated pH values, for example with a pH of more than 9 and/or temperatures above about 200°F. The deceleration mechanism of crosslinking of the organic polymer in fluids containing slightly soluble cross-linking agents based on borates, was also described to some extent. As described in U.S. patent No. 4619776, Mondshine, the unique characteristics of solubility of borates of alkaline-earth metals or borates of alkali metals alkaline earth metals give you the ability to use them for the controlled crosslinking of aqueous systems containing guar polymers. The rate of crosslinking can be controlled by a suitable control of the following variables - started the aqueous pH of the water system, the relative concentrations of one or more slightly soluble borates, the temperature of the water system and particle size borate. However, there are several limitations of using the known agents for slightly soluble borates, which are stitched suspension water-based operations gap, this particle size/concentration of solid borates and the initial pH value of the solution of guar. Currently, the main way to change the time of fusion of the liquid to be processed, using slightly soluble borate, based on the modification of the particle size borate. This technology cannot be applied to the requirement for deceleration of the stitching on 3-45 C. smaller particles can sometimes slow the stitching, but even with the use of milling and air classification particle size is not always very small in order to provide the desired quick stapling. In addition, the limited solid solubility of borates is undergoing great change as it changes the pH of the basic solution of guar. For example, when the alkalinity speed increases from a more acidic pH to an alkaline pH of 10, the time of crosslinking decreases. At pH values more than about 10 reverses the change and the stitching is slower with increasing alkalinity. In the more high is the cue of pH (for example, over 11.6), which are used to ensure the stability of the viscosity of the gel at elevated temperatures, lead time stitching over 12 min, even when using very small particles of Borat. Reduced time stitching with the use of smaller particles with a larger surface area or increased concentrations slightly soluble borates cannot be obtained due to gelation stitched concentrate, caused by the presence of a larger quantity of solid particles and their subsequent interaction. In view of the above there is a need to create compositions, systems and methods to provide more accurate control of the delay of the reaction of the crosslinking water based fluids borates for treatment of underground formations, such as the frac fluid. The invention described and disclosed in this application is directed to improved compositions and methods for the selective control of the speed of crosslinking reactions in aqueous liquids for treatment of underground formations, especially when changing pH values and in a wide temperature range in formation, including temperature over 200°F. The invention This application provides new compositions and systems for providing a controlled slow-motion stitching in aqueous solution, as well as methods of preparation and use of the x compositions, moreover, compositions containing stitched organic polymer and a crosslinking additive, consisting of slightly soluble borate crosslinking agent suspended in the aqueous modifier stitching - fully soluble salts, acids or alkaline components, which are able to regulate the rate at which gelation of the organic polymer without significant changes final pH or other characteristics of the crosslinked system. In accordance with the first variant of the present invention describes compositions for controlling the speed of gelation containing polymer fluid handling well, and the songs contain stitched organic polymer slightly soluble borate crosslinking agent and the composition of the modifier stitching, capable of controlling the rate at which cross-linking additive accelerates gelation stitched organic polymer, the modifier stitching is a salt, an alkaline or acidic agent, or a combination of both. In accordance with other non-limiting aspects of this option modifier linkage selected from the group consisting of KCO2H, KC2H3O2CH3C2H, HCO2H, KCO2H, NaCO2H, NaC2H3O2, NaCO2H and combinations thereof. According to another aspect of this is variant, the composition may further contain a chelating agent. According to another variant of the present invention describes compositions of liquids for treatment of wells comprising an aqueous solution consisting of stitched organic polymer, cross-linking additives, containing slightly soluble borate crosslinking agent and modifier stitching, while the modifier stitching able to control the rate at which slightly soluble borate accelerates gelation or crosslinking slivaushiesia organic polymer at a pH of more than about 7. In accordance with this aspect of this application modifier stitching is a salt, an alkaline or acidic compound or a combination of both. According to another variant of the present invention describes methods for treatment of underground formations, the method includes obtaining fluid for treatment of wells containing a mixture of aqueous solution and stitched organic polymer that at least partially soluble in aqueous solution; the hydration of organic polymer in an aqueous solution; preparation of cross-linking additives, including borate crosslinking agent and modifiers stitching, adding a cross-linking additive to the hydrated fluid processing so that happened controlled crosslinking of the organic polymer; and delivery of fluid for processing in the underground formation. In compliance the with other variants of the present invention describes compositions for controlling the crosslinking of aqueous solutions for the processing of wells, when this composition include stitched viscous organic polymer; slightly soluble borate crosslinking agent and modifier stitching, capable of controlling the rate at which a crosslinking agent accelerates gelation stitched organic polymer at a pH of more than about 7; and the modifier stitching is a salt, sour agent or an alkaline agent, or a combination of both. According to other aspects of this option modifier stitching has valence +1 or +2. In accordance with other non-limiting aspects of this option modifier linkage selected from the group consisting of KCO2H, KC2H3O2CH3CO2H, HCO2H, KCO2H, NaCO2H, NaC2H3O2, NaCO2H and combinations thereof. In accordance with other variations of the present invention describes the composition of fracturing fluid for use in subterranean formations, the fluid gap includes an aqueous fluid, such as water brine; stitched viscous organic polymer; slightly soluble borate crosslinking agent and the composition of the modifier stitching, which is capable of controlling the rate at which slightly soluble borate crosslinking agent knits organic polymer at pH values more than about 7. In accordance with aspects of this option modifier with the air traffic management is a salt, alkaline or acidic agent, or a combination of both. According to other aspects of this variant, the composition may also contain one or more chelating agents and/or friction reducers. Detailed description of the invention Description of specific structures and functional groups, below, does not restrict the scope of the invention or scope of the attached claims. Rather, this description is given in order to provide guidance of any specialist in this field with the purpose of implementation and enforcement of the invention which is sought patent protection. Specialists in this field will be clear that not all the characteristics of the present invention described or shown for better clarity of the invention. Experts also clear that the creation of a truly commercial variant, revealing aspects of these inventions will require many specific decisions to achieve the ultimate goal of the inventor. Such decisions may include, and not be limited to, compatibility with factors related to the system, business and government regulations, and other factors, which may differ by specific performance, place and time. Although the efforts of the developer can be time consuming and require a long time in the absolute sense, however, such efforts is Udut routine for professionals. It should be understood that the described invention is capable of various modifications and alternative forms. Finally, the application of any term in the singular does not limit the number of signs. In addition, the use of relative terms such as "top", "bottom", "left", "right", "below", "down", "up", "side", etc. is for clarity and does not restrict the scope of the invention or the claims. Applicants have developed compositions and methods for controlled fusion slivaushiesia organic polymers in liquids for well treatment, using suspensions of water-based, containing slightly soluble borates, and composition of the modifier stitching, and also suggested the use of such compositions and methods in a number of operations on allocation of hydrocarbons. In accordance with aspects of the present invention in the application described compositions of liquids for treatment of wells, which are useful in combination with the compositions and methods according to the invention and which can be used to control the speed of the stitching in liquids in a variety of subsurface environments in a wide range of pH. These compounds are liquids for processing, such as the composition of fracturing fluids contain at least a water-based liquid, stitched organic polymer slightly soluble borate with ivaldi agent and the composition of the modifier stitching, when this modifier stitching able to control the speed with which slightly soluble borate crosslinking agent accelerates gelation of the organic polymer at a stable pH of more than about 7. In accordance with one variant of the present invention compositions and systems with controlled stitching can be applied when conducting operations on the allocation of underground hydrocarbons, when the composition or system is in contact with the underground formation, in which the temperature ranges from about 150°F (66°C) up to about 500°F (260°C), including the interval from about 170°F (77°C) to 450°F (232°C) and from about 200°F (93°C) up to about 400°F (204°C). Typical stitched organic polymers, sometimes referred to in this application as "agent, forming a gel that can be included in the fluid and system for processing described here, in particular aqueous fluid system, and which can be used in the invention typically include biopolymers, synthetic polymers, or a combination, and agents, forming a gel or stitched organic polymers at least partially slightly soluble in water (the term "slightly" means a solubility of at least about 0.01 kg/m3). Without limitation, these stitched organic polymers can serve to increase elm the spine of fluid for processing during its application. According to the methods and compositions of the invention can be applied to various gelling agents, including, but without limitation, hydradermie polymers that contain one or more functional groups such as hydroxyl, ishigakijima, carboxyl, groups, derivatives of carboxylic acids, sulfate, sulphonate, phosphonate or amide. Gelling agents may also be biopolymers, including natural, modified and derivationally polysaccharides and derivatives thereof that contain one or more monosaccharide units selected from the group comprising galactose, mannose, glucoside, glucose, xylose, arabinose, fructose, glucuronic acid or peresilalas. Suitable gelling agents that may be used in accordance with this invention also include, but without limitation, guar, hydroxypropanoyl (HPG), cellulose, carboxymethylcellulose (CMC), karboksimetiltselljuloza (SMES), hydroxyethyl cellulose (HEC), carboxyphenoxypropane (CMHPG), other derivatives of the guar gums, xanthan gum, galactomannan resin and resin, comprising galactomannan, cellulose and other cellulose derivatives, and combinations thereof, such as various esters of karboksimetsiltsellyulozy, such as karboksimetilcelljuloza; mixed ethers such as carbox alkylether; hydroxyethylcellulose, such as hydroxypropylcellulose; alkylhydroxylamines, such as methylhydroxypropylcellulose; alkylaryl, such as methylcellulose, ethylcellulose and propylethylene; alkylcarboxylic, such as ethylcarboxylate; alkylalkoxysilane, such as metilcellulose; hydroxyethylmethylcellulose, such as hypromellose; combinations thereof and the like, Preferably according to one non-limiting variant of this invention, the gelling agent is guar, hydroxypropanoyl (HPG) or carboxyphenoxypropane (CMHPG) individually or in combination. Other natural polymers suitable for use as the stitching of organic polymer/gelling agents according to this invention include, but without limitation, the resin carob, gum packaging (Cesalpinia spinosa lin), resin elephant Yam (Amorphophallus konjac), starch, cellulose, gum karaya, xanthan resin, tragacanth gum, resin acacia, gum, ghatti, resin tamarind, carrageenan and derivatives thereof. In addition, synthetic polymers and copolymers that contain any of the aforementioned groups may also be used. Examples of such synthetic polymers include, without limitation, polyacrylate, polymethacrylate, high is, polyvinyl alcohol, copolymers of maleic anhydride, copolymers metilfenidato ether and polyvinylpyrrolidone. In General, the amount of gelling agent/stitched organic polymer that may be included in the composition of the liquid for processing according to the invention depends on the desired viscosity. The amount of this agent must be effective to achieve the desired viscosity. According to some variants of these inventions gelling agent may be contained in the fluid to be processed in the amount of from about 0.1% to about 60% based on the weight of the liquid to be processed. According to other variants of gelling agent may be contained in an amount of from about 0.1% to about 20% based on the weight of the liquid to be processed. In General, however, the number of stitched organic polymer included in the liquid for treatment of wells described in this application is not critical as long as the viscosity of the liquid is high enough to keep the particles of propping agent or other additives suspended in the fluid during the phase of injection of fluid into an underground formation. So, depending on the particular application liquid for processing for stapling the organic polymer may be added to liquid water-based concentrations from about 15 is about 60 pounds per thousand gallons (pptg) by volume based on the water-based liquid (1,8-7,2 kg/m 3). According to another variant of this concentration can range from about 20 pptg (2.4 kg/m3) to about 40 pptg (4.8 kg/m3). In accordance with other non-limiting aspects of the present invention, the number of stitched organic polymer/gelling agent contained in the liquid water-based, can range from about 25 pptg (about 3 kg/m3) to about 40 pptg (about 4.8 kg/m3) per volume of liquid. The person skilled in the art from consideration of this application may determine the type of the desired gelling agent and its amount for particular application. Preferably, in accordance with one aspect of the present invention the liquid composition or system for processing wells will contain from about 1.2 kg/m3(0,075 f/ft3) to about 12 kg/m3(0,75 f/ft3) gelling agent/stitched organic polymer, most preferably from about 2.4 kg/m3(0,15 f/ft3) to about 7.2 kg/m3(0,45 f/ft3). Composition modifiers stitching, suitable for introduction to fluid processing according to this invention, include one or more additives to control the stitching, which is preferably selected from the group consisting of acidic agents, alkaline agents, salts, combinations of these agents (e.g., salts and the Christmas tree agents), the combination of which can also serve as a reducer of the freezing point. Fluid freezing point by themselves can also be included in the composition of a crosslinking additive according to the invention individually and separately from the modifiers bound. Acidic agents that can be used as modifiers staple according to this invention include inorganic and organic acids, and combinations thereof. Examples of suitable acidic agents include acetic acid (CH3CO2H), boric acid (H3BO3), carbonic acid (H2CO3), hydrochloric acid (HCl), nitric acid (HNO3), gaseous hydrochloric acid (HCl gas), perchloro acid (HClO4), Hydrobromic acid (HBr), yodiewonderdog acid (HI), phosphoric kisitu (H3PO4), formic acid (HCO2H), sulfuric acid (H2SO4), forcerenew acid (FSO3H), forcerenew acid (HFSbF5), p-toluensulfonate (pTSA), triperoxonane acid (TFA), triftormetilfullerenov (CF3SO3H), econsultation, methanesulfonate (MSA), malic acid, maleic acid, oxalic acid (C2H2O4), salicylic acid, triftormetilfullerenov, citric acid, succinic acid, tartaric acid and heavy sulfate total of four who uly XHSO 4(where X denotes an alkaline metal such as Li, Na and K). Alkaline agents, which can be used as modifiers stapling in accordance with this invention include, but without limitation, inorganic and organic alkaline agents (bases), and their combinations. Examples of alkaline agents suitable for this application include, but without limitation, amines and nitrogen-containing heterocyclic compounds such as ammonia, methylamine, pyridine, imidazole, histidine, and benzimidazole; hydroxides of alkali metals and alkaline earth metals, including, but without limitation, potassium hydroxide (KOH), sodium hydroxide (NaOH), barium hydroxide (Ba(OH)2)), cesium hydroxide (CsOH), strontium hydroxide (Sr(OH)2), calcium hydroxide (CA(OH)2)), lithium hydroxide (LiOH) and rubidium hydroxide (RbOH); oxide such as magnesium oxide (MgO), calcium oxide (CaO) and barium oxide; carbonates and bicarbonates of alkali metals, alkaline earth metals and transition metals, including sodium bicarbonate (NaHCO3), sodium carbonate (Na2CO3), potassium carbonate (K2CO3), potassium bicarbonate (KHCO3), lithium carbonate (LiCO3), carbonate, rubidium (Rb2CO3), cesium carbonate (CS2CO3), beryllium carbonate (BeCO3), magnesium carbonate (MgCO3), calcium carbonate (CaCO3), carbonate stronz is I (SrCO 3), barium carbonate (BaCO3), manganese carbonate (II) (MnCO3), carbonate iron (II) (FeCO3)carbonate cobalt (CoCO3)carbonate Nickel (II) (NiCO3)carbonate copper (II) (CuCO3), zinc carbonate (ZnCO3), silver carbonate (Ag2CO3), cadmium carbonate (CdCO3and carbonate of lead (Pb2CO3); phosphate salts such as potassium dihydrophosphate (KH2PO4), monohydratefast of dicale (K2HPO4and rejonowy phosphate potassium (K3PO4); the acetates of alkali metals, alkaline earth metals, and transition metals, such as potassium acetate (KC2H3O2), sodium acetate, lithium acetate, rubidium acetate, cesium acetate, beryllium acetate, magnesium acetate, calcium acetate, calcium acetate-magnesium, strontium acetate, barium acetate, aluminum acetate, acetate, manganese (III)acetate, iron (II)acetate, iron (III), cobalt acetate, Nickel acetate, copper acetate (II), chromium acetate, zinc acetate, silver acetate, cadmium acetate, and the acetate of lead (II); the formate of alkali metals, alkaline earth metals and transition metals, such as formate potassium (KCO2H), sodium formate (NaCO2H) and cesium formate (CsCO2H); and alkoxides (base alcohol), including, but without limitation, sodium alkoxide, potassium alkoxide, trebuetsya potassium, isopropoxide titanium (Ti(OCH(CH3)2)4), from robaxin aluminum (Al(O-i-Pr) 3where i-Pr means isopropyl group (- CH(CH3)2and tetraethylorthosilicate (TEOS, Si(OC2H5)4)). Salts that can be used as modifiers staple according to the invention, include, but without limitation, as inorganic salts, such as salts of alkali metals, salts of alkaline earth metals and salts of transition metals, such as salts of halide compounds, for example sodium chloride, potassium chloride, magnesium chloride, calcium chloride and zinc chloride, and organic salts such as sodium citrate. The term "salt (salt)" means as acidic salts formed with inorganic and/or organic acids, or basic salts formed with inorganic and/or organic bases. Examples of acid salts of joining include acetates such as potassium acetate, ascorbate, benzoate, benzoylformate, bisulfate, borates, butyrate, citrates, camphorate, campanulate, fumarate, hydrochloride, hydrobromide, hydroiodide, lactates, maleate, methanesulfonate, naphthalenesulfonates, nitrates, oxalates, phosphates, propionate, salicylates succinate, sulphates, tartratami, thiocyanates, toluensulfonate (also known as tozilaty), etc. Examples of basic salts include ammonium salts, alkali metal salts, such as salts of sodium, lithium and potassium, salts of alkaline earth metals, such the as calcium salts and magnesium, salts of organic bases (for example, organic amines such as dicyclohexylamine, tert, butylamine, and salts with amino acids such as arginine, lysine and the like). Basic nitrogen-containing groups of organic compounds can be quaternidinum using agents such as gelidity lower Akilov (for example, methyl-, ethyl - and butylchloride, bromides and iodides), diallylsulfide (for example, dimethyl-, diethyl - and dibutylaniline), gelidity long chains (e.g., decyl-, lauryl -, and stearylamine, bromides and iodides), aralkylated (for example, benzyl and peptibody) and other, forming a basic organic salt. Used in this application, the term "alkali metal" refers to a group of elements comprising Group 1 of the Periodic table of elements, and the term "alkaline earth metal" refers to elements that make up Group 2 of the Periodic table of elements, the Group 1 and Group 2 defined by the International Union of Pure and Applied Chemistry (2002). Preferred modifiers stitching, suitable for use in the described compositions are carbonates of alkali metals, formate, alkali metal acetates, alkali metals and hydroxides of alkali metals. Typical modifiers stapling include potassium carbonate, potassium formate, potassium acetate, potassium hydroxide, and combinations thereof. In accordance the with one aspect of the present invention modifier stitching represents a monovalent salt, the acidic agent and an alkaline agent, which lowers the freezing point of the aqueous composition, such as lithium salts, sodium, potassium or cesium, acidic agents or alkaline agents. In accordance with another aspect of the present invention modifier stitching represents a divalent salt, sour agent or an alkaline agent, which lowers the freezing point of the aqueous composition, such as calcium salts or magnesium, acidic agents or alkaline agents. Fluid freezing temperature, which can be used as modifiers stapling in accordance with aspects of the present invention include, but without limitation, metal salts, including alkali metal salts, alkaline earth metals and transition metals with organic acids, linear sulfonates, metal salts and Caprylic acid, polyamide succinic acid and their salts, metal salts and N-laurylsarcosine, alkylnaphthalene, polymethacrylates, such as Viscoplex®[Rohm RohMax] and LZ®V, 7742 and 7748 [all Lubrizol Corp.], the vinyl acetate, finishment, copolymers of styrene with maleic anhydride and other fluid freezing point, known from the prior art. The amount of modifier recent compositions, crosslinking additives ranges from about 0.01 wt.% to about 80 wt.% from the weight of the solution and, more preferably, from about 0.1 wt.% to p is IMEMO 65 wt.%. The amount of modifier used, the stitching may be determined from the ratio of modifier stitching and slightly soluble borate crosslinking agent comprising from about 1:1 to about 10:1, more preferably from about 1:1 to about 5:1, including relationships within their intervals, such as about 2:1, about 2.5:1, about 3:1, about 3.5:1, about 4:1 and about 4.5:1, inclusive. The main liquid composition for treatment of wells used in the compositions and methods according to the invention preferably is a water-based liquid, although it can also be a liquid oil-based or emulsion. The primary fluid may be from any source provided that it does not contain compounds that may adversely affect other components of the composition for treatment. The primary fluid may be natural or synthetic origin. According to some variants of these inventions, the water-based liquid can be a plain water or salt water depending on the desired density of the composition. The term "salt water" can mean the water is not saturated with salts or saturated salts "system brines", such as brine NaCl or KCl brine and heavy brines, including salt CaCl2, CaBr2and KCO2H. Brines, suita is included for use, can contain from about 1 % to about 75% of the weight of the corresponding salts, including about 3 wt.%, about 5 wt.%, about 10 wt.%, about 15 wt.%, about 20 wt.%, about 25 wt.%, about 30 wt.%, about 35 wt.%, about 40 wt.%, about 45 wt.%, about 50 wt.%, about 55 wt.%, about 60 wt.%, about 65 wt.%, about 70 wt.% and about 75 wt.%, without restrictions, as well as concentrations between any two of these values, for example from about 21 wt.% to about 66 wt.%, inclusive. In General, the primary fluid in the fluid for the well treatment is contained in an amount of from about 2% to approximately 99.5% by weight. According to other variants of the main liquid is contained in an amount of from about 70% to about 99% by weight. Depending on the desired viscosity of the composition for processing in its composition include more or fewer of the base fluid. The person skilled in the art given this description can easily determine the type of the base fluid and the amount for use under this application. In accordance with the example methods according to the invention an aqueous liquid gap can be obtained, without limitation, by mixing one or more stitched organic polymers in aqueous base fluid. Water is the main liquid may represent, for example, water, brine (e.g., brine NaCl or KCl) foam water-based or a mixture of water and alcohol. The brine may be of any prepared or obtained for this purpose, and serves as a suitable environment for the various components. For convenience, in many cases, the brine may be, for example, any brine that is available for use in the liquid to complete the well. For this receive operation can be applied to any apparatus for mixing. In the case of periodic mixing stitched organic polymer, such as guar or its derivative, and the aqueous liquid are mixed for a period of time sufficient for the formation of generowania or become viscous solution. The organic polymer suitable according to the invention preferably represents any of hydroceramic polysaccharides described above, and in particular those hydratherapie polysaccharides, which are capable of forming a gel in the presence of a crosslinking agent with the formation of a gel-like base fluid. The most preferred hydratherapie polymers according to this invention are guar gum, carboxyphenoxypropane and hydroxypropanoic, and their combinations. According to other variants of the present invention stitched organic polymer or gelling agent may be depolymerization if necessary. The term "depolimerizovannogo" usually refers to decrease the structure of the molecular weight gelling agent. Depolimerizovannogo polymers described in U.S. patent No. 6488091, the content of which is incorporated in this application by reference. In addition to the main water liquid and stitched organic polymer fluid for the well treatment contains a crosslinking agent used for crosslinking of the organic polymer and receiving becomes a viscous liquid for processing. Although it may be applied to any cross-linking agent, it is preferable that this crosslinking agent represented slightly soluble borate. For the purposes of this invention, the term "slightly soluble" means an agent having a solubility in water at a temperature of 22°C (71,6°F) less than 10 kg/m3defined by the known methods such as described Gulensoy, et al. [M.T.A.Bull., No. 86, p.77-94 (1976); M.T.A.Bull., no.87, pp.36-47 (1978)]. For example, without limitation, reasonable slightly soluble borates to the water solubility at a temperature of 22°C (71,6°F) in the range of about 0.1 kg/m3up to about 10 kg/m3. Generally, in accordance with this invention slightly soluble borate crosslinking agent can be any compound which provides a solution of borate ions and/or their releases. Examples slightly soluble borates, suitable as cross-linking agents in the compositions according to the invention, include, but without limitation, boric acid, borates, alkali metal borates school is full - time - alkaline earth metals and the alkaline earth metal borates, such as the tetrahydrate of dynatricarbonate, Deborah sodium, and boron-containing minerals and ores. In accordance with some aspects of the present invention, the concentration of slightly soluble borate crosslinking agent as described in this application, a liquid for processing is in the range from about 0.01 kg/m3up to about 10 kg/m3preferably from about 0.1 kg/m3to about 5 kg/m3and more preferably from about 0.25 kg/m3to about 2.5 kg/m3. Boron minerals, suitable for use as a slightly soluble borate crosslinking agent according to this invention, are ores containing 5 wt.% or more of boron, including minerals and ores of natural origin and synthetic minerals and ores. Examples of natural boron-containing minerals and ores, suitable for use include, but are not limited to, boron oxide (B2O3), boric acid (H3BO3), borax (Na2B4O - 10 H2O), colemanite (Ca2B6O11- 5 H2O), Frolova (Ca2B4O8- 7 H2O), generic (Ca2B14O23- 8 H2O), goferit (CaB6H10- 5 H2O), holic (Ca4B10O23Si2- 5 H2O), hydroboracite (CaMgB6O 11- 6 H2O), anderbolt (CaMgB6O11- 11 H2O), Indesit (Mg2B6O11- 15 H2O), injoit (Ca2B6O11- 13 H2O), calibret (Heintzite) (KMg2B11O19- 9 H2O), cernet (ruin) (Na2B4O7- 4 H2O), kurnakovite (MgB3O3(OH)5- 15 H2O), meyerhofferite (Ca2B6O11- 7 H2O), noblet (CaB6O10- 4 H2O), pandemic (Ca4B10O19- 7 H2O), paternot (MgB2O13- 4 H2O), Pinot (MgB2O4- 3 H2O), priceit (Ca4B10O19- 7 H2O), preobrajenska (Mg3B10O18to 4.5 H2O), probertite (NaCaB5O9- 5 H2O), artsit (Ca4B10O19- 20 H2O), tincalconite (Na2B4O7- 5 H2O), tunellite (SrB6O10- 4 H2O), ulexite (Na2Ca2B10O18- 16 H2O), veatchite (Sr4B22O37- 7 H2O), as well as any of borates class V-26 to Dana Classification, hydrated borates containing hydroxyl groups or halogen atoms, described in Gaines, R.V., et al. [Dana''s New Mineralogy, John Wiley & Sons, Inc., NY, (1977)], or borates class V/G V/H, V/J or V/K according to the classification system of Stronza [Hugo Strunz; Ernest Nickel: Strunz Mineralogical Tables, Ninth Edition, Stuttgart: Schweizerbart, (2001)]. Any of these borates can be gidratirovannym is to contain variable amounts of hydration water, including, but without limitation, tetrahydrate, palpitate, sesquihydrate and pentahydrate. In addition, in accordance with some aspects of the present invention preferably slightly soluble borates were borates containing at least 3 of the boron atom in the molecule, for example, were triborate, tetraborate, pentaborate, hexaborate, heptanoate, decaborate, etc. In accordance with one aspect of the present invention, the preferred cross-linking agent is slightly soluble borate selected from the group consisting of ulexite, colemanite, probertite and mixtures thereof. Synthetic slightly soluble borates, which can be used as cross-linking agents described in liquids for treatment of wells and in the implementation of the methods according to the invention, include, but are not limited to, noblit and hoverit, which can be obtained by known methods. For example, obtaining synthetic colemanite, inyoite, gowerite and meyerhofferite described in U.S. patent No. 3332738, U.S. Nary Department, according to which the sodium borate or boric acid react with such compounds as CA(IO)2, CaCl2, Sa(C2H3O2)2within 1-8 days. Synthesis of ulexite from boraxo and CaCl2has also been described [Gulensoy, N., et al., Bull. Miner. Res. Explor. Inst. Turk., Vol.86, p.75-78 (1976)]. Synthetic noblit can be obtained g is Kotelnicheskaya processing meyerhofferite (2CaO 3BrO3- 7 H2O) in a solution of boric acid for 8 days. at a temperature of 85°C, as described in patent No. 3337292. Noblit can also be obtained in accordance with the methods Erd. McAllister and Vlisidis [American Mineralogist, Vol.46, pp.560-571 (1961)], which describes the synthesis of nobleite by mixing CaO and boric acid in water for 30 hours at a temperature of 48°C, followed by exposure of the resulting product at a temperature of 68°C for 10 days. Other methods that can be used to produce synthetic boron-containing materials used in the method according to this invention, include hydrothermal methods described, for example, Yu, Z. - T., et al. [J. Chem. Soc, Dalton Transaction, pp.2031-2035 (2002)], and Sol-gel method (see, for example, Komatsu, R., et al., J. Jpn. Assoc. Cryst. Growth., Vol.15, p.12-18 (1988)] and the method of fusing. However, although slightly soluble synthetic borates can be used in the compositions and liquids for treatment of wells described in this application, preferred are slightly soluble borates of natural origin. This is partly due to the fact that, although synthetic compositions may have a higher degree of purity than natural materials, because they do not contain impurities contained in natural materials, they are typically characterized by a lower content of borates. The number of ions is orata in the solution for treatment often depends on the pH of the solution. According to one non-limiting variant of this invention, the crosslinking agent preferably represents one of boron-containing ores selected from the group consisting of ulexite, colemanite, probertite and mixtures thereof, contained in amounts ranging from about 0.5 to about 45,0 pptg (pounds per thousand gallons) of fluid for treatment of wells. According to another non-limiting variant, the concentration of slightly soluble borate crosslinking agent is in a liquid for processing in the range of about 3,0 pptg to about of 20.0 pptg. The composition of the invention can optionally contain other optional additives, if this is desirable or optional, which include, but without limitation, suspendresume agents (agents that prevent the deposition, the stabilizers deflocculant, thinners, chelating agents) binding compounds, non-emulsifiers, additives that prevent the loss of fluids, biocides, propping agents, buffer agents, additives, weighting materials, wetting agents, lubricating agents, friction reducers, antioxidants, agents for controlling the pH value, oxygen scavengers, surfactants, stabilizers, small particle, chelating agents for metals, complexing agents metals, antioxidants, stabilizers, polymers, stabilizers is Lina, fluid freezing point, inhibitors of salt deposits, the solvent for salt deposits, shale inhibitors, corrosion inhibitors, inhibitors of waxes, solvents for waxes, inhibitors, asphaltene precipitation inhibitors of the water injection, the agents for strengthening of sand, agents, controlling the leakage of fluid, permeability modifiers, microorganisms, as well as viscoelastic liquids, gases, foaming agents, nutrients for microorganisms, and combinations thereof, provided that none of these optional additives does not impact adversely on other components. When implementing the methods and compositions according to the invention to reduce or dissolution of the gel in the liquid can be applied to various thinners, including, but without limitation, enzymes, oxidizing agents, polyols, aminocarbonyl acid, etc. together with additives that contribute to liquefaction of the gel. The person skilled in the art can easily choose the type of additives, suitable for carrying out specific processing operation of the underground formation. In addition, all such possible additives can be included, if necessary, provided that they do not destroy the structure, stability, does not harm the mechanism controlled deceleration or subsequent destruction crosslinked gels at the end of their use. In accordance with typical what spectale of this invention, a crosslinking agent (or agents) is supported in a suspended state in the cross-linking additive due to the inclusion of one or more suspendida cross-linking agents in the composition. Suspendisse agent generally increases the viscosity of the liquid and prevents the precipitation of the cross-linking agent. Suspendresume agents can also minimize syneresis, the separation of a liquid medium, which leads to the formation of a layer on top of a concentrated cross-linking additives during aging. Suitable for use according to this invention suspendresume agents include solids with high specific gravity and low specific gravity, the latter may include active agents such as clays, polymers, and combinations thereof, and inactive solids. According to non-limiting aspect of the present invention suspendium agent can be any suitable clay, including, but without limitation, palygorskite clays, such as hectorite, montmorillonite, kaolinite, saponite, bentonite, and combinations thereof, fallerovo earth, mica, such as Muscovite and phlogopite and synthetic clays, such as laponite. Suspendisse agent may also be a water-soluble polymer, which will hydrogenate itself in liquids for processing described in this application. Suitable water-soluble polymers that can be used in liquids for treatment include, but without limitation, synthesized biopolymers, such as xanthan gum, cellulose derivatives, natural polymers and/or derivatives of ubago of these water-soluble polymers, such as gums derived from plant seeds. In the crosslinking of the compositions according to the invention can be applied to different combinations of these suspendida agents. Preferably according to some aspects of the present invention suspendisse agent is a clay selected from the group consisting of attapulgite, sepiolite, montmorillonite, kaolinite, bentonite, and combinations thereof. The amount of suspending agent, which may be included in the cross-linking additives described in this application is from about 1 pound per barrel (42 gallons) to about 50 pounds per barrel (ppb) or more preferably from more than 2 pounds per barrel to about 20 pounds per barrel, including approximately 3 ppb, approximately 4 ppb, about 5 ppb, approximately 6 ppb, approximately 7 ppb, about 8 ppb, about 9 ppb, 10 ppb, about 11 ppb to about 12 ppb, about 13 ppb, about 14 ppb, 15 ppb, approximately 16 ppb, about 17 ppb, about 18 ppb, approximately 19 ppb, including values between any two of these values, for example from about 2 ppb to about 12 ppb inclusive. It should be noted that for the purposes of this invention 1 pound mass lbm/bbl is equivalent to one pound of additives in 42 gallons of liquid (USA); it should be noted that lbm/bbl can be written as PPB or ppb, but this reduction should not be confused with the "parts per billion" (ppb). In SI units: one f is HT/barrel equal to 2.85 kg/m 3such as 10 pounds of weight / bbl=28.5 kg/m3. Deflocculant is a thinning agent used to reduce the viscosity or prevent flocculation, it is sometimes called (incorrectly) "dispenser". The majority of deflocculants are nizkomolekulyarnymi anionic polymers, which neutralize the positive charges on the clay particles. Examples of suitable deflocculants include, but without limitation, polyphosphates, lignosulfonates, quebracho (powder form of the extract tanimowo acid from the bark of a tree quebracho used as deflocculant lime solution with a high pH) and various water-soluble synthetic polymers. Aqueous fluid for the well treatment according to this invention may contain predominantly contain one or more friction reducers in amount from about 10 wt.% to about 95 wt.%. Used the term "friction reducer" refers to the chemical additives that reduce friction loss due to friction between water liquid for processing in a turbulent flow and tubular elements (e.g., pipes, coils and so on) and/or formation. Suitable friction reducers used in the compositions of aqueous liquids for processing according to this invention, include, but are not limited to, odorant orime non-ionic compounds, such as polyalkylene glycols and polyethylene oxide, and polymers and copolymers, including, without limitation, (co)polymers of acrylamide, poly(dimethylaminoethylacrylate), sodium salt polystyrenesulfonate and combinations thereof. In accordance with this aspect of the invention, the term "copolymer" is not limited to polymers containing two types of monomer units, but includes any combination of monomer units, for example ternary polymers, terpolymer etc. In accordance with certain non-limiting aspects of the present invention described aqueous fluid for the well treatment may optionally include one or more chelating agents to reduce the cases, when there is an adverse effect on the controlled crosslinking of solutions, for example, to reduce the incidence of water pollution. Used in this application, the term "chelating agent" refers to compounds containing one or more donor atoms, which may be connected by coordinate bonding with a single metal ion with the formation of a cyclic structure, also known as chelating complex or chelate, thereby inactivating metal ions so that they cannot react normally with other elements or ions with obtaining precipitation or sediment. So, don't chelates have the structural characteristics of one and the and multiple coordination bonds, formed between a metal ion and two or more atoms in the molecule chelating agent, also called the "ligand". Suitable chelating agents used according to the invention can be monodentate, hexadentate, octodentata, etc. without limitation. The amount of chelating agent used in the compositions described in this application will depend on the type and quantity of ion or ions, which gelatinous or contact. When chelating agents are included in the compositions according to the invention, it is preferred that the pH of liquids for treatment of wells described in this application was equal to the value that higher pH, which will precipitate the free acid chelating agent; in General, the pH should be above about 1 to deliver fluid to process down. Examples of chelating agents suitable for use in the compositions and liquids for processing according to the invention, include, but without limitation, acetic acid, acrylic polymers, aminopolycarboxylate acids and phosphonic acids and their sodium, potassium and ammonium salts, ascorbic acid, BayPure®CX 100 (tetranitro iminodisuccinate available at LANXESS Corporation, Pittsburgh, PA) and similar biodegradable chelating agents; carbonates such as sodium carbonate and potassium; citric acid; decarboxylation the new acid; aminopolycarboxylate acid, including, but without limitation, cyclohexyldiazeniumdioxy acid (CDTA), diethylenetriaminepentaacetic acid (DTPA), ethylenediaminetetra acid (EDDS), ethylenediaminetetraacetic acid (EDTA), hydroxyethylation diaminetetraacetic acid (HEDTA), hydroxyethylaminophenol acid (HEIDA), nitryltriacetic acid (NTA) and sequentialy salt diethylenetriaminepenta (methylenephosphonic) acid (DTPMP-Na7or mixtures thereof; inulin (for example, carboxymethyllysine sodium); malic acid, non-polar amino acids such as methionine and the like; oxalic acid, phosphoric acid, phosphonates, in particular organic phosphonates, such as aminotris-methylenephosphonate sodium; phosphonic acids and their salts, including, but without limitation ATMP (aminotri-(methylenephosphonic acid)), HEDP (1-hydroxyethylidene-1,1-phosphonic acid), HDTMPA (hexamethylenediaminetetra-(methylenephosphonic acid)), DTPMPA (diethylenetriaminepenta-(methylenephosphonic acid)and 2-phosphonobutane-1,2,4-tricarboxylic acid, such as commercially available DEQUEST™ phosphonates (Solutia Inc., St. Louis, MO); phosphate esters; polyaminocarboxylic acid; polyacrylamide; polycarboxylic acids; polysulfone acid; esters of phosphates, inorganic phosphates; polyacrylic acid; phytic acid and its derivatives (especially carboxy is contains); polyaspartate; polyacrylates; polar amino acids (and the alpha and beta forms), including, but without limitation, arginine, asparagine, aspartic acid, glutamic acid, glutamine, lysine and ornithine; siderophore, including, but without limitation, desferrioxamine of siderophore Desferrioxamine B (DFB-specific agent that forms a complex with iron, obtained from metabolite Actinomycetes (Streptomyces pilosus), carrying the iron atoms and cyclic trihydroxy produced P.stutzeri, Desferrioxamine E (DFE)); succinic acid; trihydroxyphenyl acid and its derivatives, and combinations the above chelating agents and free acid such chelating agents and water-soluble salts (for example, Na+-, K+-, NH4+and CA2+-salt). Non-limiting examples of chelating agents, metal complexes, which are used according to this invention and which form complexes with suitable metal ions include chelates of salts of barium (II), calcium (II), strontium (II), magnesium (II), chromium (II), titanium (IV), aluminum (III), iron (II), iron (III), zinc (II), Nickel (II), tin (II) or tin (IV) and complexes with nitryltriacetic acid, 1,2-cyclohexanediamine-N N,N',N'-tetraoxane acid, diethylenetriaminepentaacetic acid, Ethylenedioxy-bis-(athienitis) tetraoxane acid, N-(2-hydroxyethyl)-ethylendiamine-N,N',N'-three is kusnoy acid, Triethylenetetramine acid or H-(hydroxyethyl)-ethylenediaminetriacetic acid or mixtures thereof as a ligand. The fluid for the well treatment according to this invention may also optionally include propping agents for use in subterranean formations, for example, in the case of hydraulic fracturing. Suitable propping agents include, but are not limited to, gravel, natural sand, quartz sand, particles of granite, glass, ground walnut shell granules of nylon, aluminum pellets, bauxite, ceramics, polymeric materials, combinations thereof and the like, all of these agents may contain a coating based resins, reagents, giving stickiness, surface modifiers, and combinations thereof. If such coatings are used, they must not interact with the particles of propping agent or any other components of the fluid processing according to this invention. The person skilled in the art given this description can easily determine the right type, particle size and quantity of particles of the proppant used in liquids for the well treatment according to the invention, to achieve the desired result. In accordance with non-limiting variant of the applied particles of propping agent can be included in the composition of the liquid d is I the well treatment according to the invention with the purpose of obtaining gravel packing in the well or wedging operation hydraulic fracturing. Fluid processing according to this invention can optionally contain one or more pH buffers, if necessary, depending on the characteristics of underground formations that will be treated. The buffer pH is usually included in the liquid for processing according to the invention to maintain the pH in the desired range, among other things, to improve the stability of the liquid to be processed. Examples of suitable pH buffers include, but without limitation, alkaline buffers, acidic and neutral buffers buffers. Alkaline buffers include buffers, which are, without limitation, the carbonates of ammonium, potassium and sodium, bicarbonate, sesquicarbonate and acidic phosphates in amounts sufficient to provide a pH in the liquid for processing more than about 7, more preferably from about 9 to about 12. Other examples of alkaline pH buffers include sodium carbonate, potassium carbonate, sodium bicarbonate, potassium bicarbonate, sodium diacetate or potassium phosphate, sodium or potassium acid phosphate, sodium or potassium dihydrogen phosphate, sodium or potassium borate, sodium diacetate, sodium or ammonium, or combinations thereof and the like According to the invention, the pH value is not modified and remains in the liquid for processing equal to the desired value. Acidic buffers can also be used in liquids for processing is about invention. Acidic buffer solution has a pH less than 7. Acidic buffer solutions can be derived from a weak acid and one of its salts such as sodium salt, or can be purchased. An example is a mixture of ethanoic acid and ethanoate sodium in solution. In this case, if the solution containing equal molar concentrations of acid and salt, it will have a pH value equal to the value of 4.76, thus, used "acid buffer" means a compound or compounds which, when added to aqueous solution, reduce the pH value and provide resistance to the resulting solution to increase the pH when the solution is mixed with a solution with a higher pH value. Acidic buffer must have a pKa less than about 7. Some preferred intervals pKa of the acidic buffer is below about 7, below about 6, below about 5, below about 4 and below about 3. Acidic buffers with values and intervals pKa less than about 7 are included in the scope of this invention. Examples of acidic buffers suitable for use in liquids for processing described in this application include, but are not limited to, phosphate, citrate, ISO-citrate, acetate, succinate, ascorbic, formic, lactic, sulfuric, hydrochloric, nitric, benzoic, boric, butyric, Caproic, Caprylic, coal, carbon, oxalic acid, pyruvic acid, phthalic, adipic, citramalate, Umarova, glycolic, tartaric, savenow, lauric, maleic, sablotny, malonic, Orotava, propionic, methylpropionate, polyacrylic, succinic, salicylic, 5-sulfosalicylic, Valerian, isovalerianic, uric acid, and combinations thereof, such as a combination of phosphoric acid and one or more sugars, which has a pH value between about 1 and about 3, and other suitable acids and bases known in the art and are described in Kirk-Othmer Encyclopedia of Chemical Technology, 5thEdition, John Wiley & Sons, Inc., (2008). Other suitable acidic buffers are mixtures of acid and one or more salts. For example, acidic buffer, suitable for use according to the invention can be obtained by using potassium chloride or acid phosphate potassium in combination with hydrochloric acid in appropriate concentrations. The composition of aqueous fluids for processing according to the invention may also include oxygen scavengers. Used in this application, the term "oxygen scavenger" refers to those chemical agents that react with the dissolved oxygen (O2) in solution in order to reduce corrosion occurring under the action of dissolved oxygen (ion sulfite and/or bisulfite, connecting with oxygen to form sulfate) or enhanced oxygen. Oxygen scavengers usually there is a process by capturing oxygen or the formation of a complex with the dissolved oxygen in the liquid, circulating in the wellbore, a harmless chemical reaction that makes oxygen available for reaction corrosion. Examples of oxygen absorbers suitable for use in the invention include, but without limitation, metal-containing agents, such as ORGANOTIN compounds, compounds of Nickel, copper compounds, compounds of cobalt and the like; hydrazines; ascorbic acid; sulfates such as pentahydrate sodium thiosulfate; sulfites such as potassium bisulfite, potassium metabisulfite, and sodium sulfite; and combinations of two or more of these oxygen absorbers; their choice depends on the specific characteristics of the underground formation to be processed fluid processing according to the invention. To improve the solubility of oxygen absorbers, such as douglaston tin or other suitable agents, so that they could easily communicate with the compositions according to the invention in the process, the absorber(s) of oxygen can be pre-dissolved in an appropriate aqueous solution, for example, when the oxygen scavenger is used douglaston tin, it can be dissolved in dilute aqueous acid solution (e.g., a salt) with the appropriate concentration (for example, from about 0.1 wt.% up to about 20 wt.%) prior to the introduction of a liquid for processing skvazhina invention. Other conventional additives which can be used in liquids for treatment of wells described in this application include gel stabilizers that stabilize the crosslinked organic polymer (typically a polysaccharide crosslinked borate) in a period of time sufficient for injection of fluid into the desired subterranean formation. Suitable stabilizers crosslinked gels, which can be used in liquids for treatment include, without limitation, sodium thiosulfate, diethanolamine, triethanolamine, methanol, hydroxyethylation, Tetraethylenepentamine, Ethylenediamine and mixtures thereof. The composition of the invention may also include one or more thinners gel added at the appropriate time during processing of the underground formation. Usually once the proppant is placed in the underground passage with subsequent rupture, cross-linked liquid holding proppant (such as described above)should be diluted and macromolecular precipitation on the surface of the gap must be destroyed in order to facilitate cleaning to obtain from the formation. Usually this is done with thinners gel" chemical agents "break" molecules cross-linked polymer into smaller pieces with a lower molecular weight, providing a controlled transformation of a viscous fluid (such as liquid gap) in men is e viscous liquid, you can get from formation [see, e.g., Ely, J. W., Fracturing Fluids and Additives, in Recent Advances in Hydraulic Fracturing, Society of Petroleum Engineers, Inc.; Gidley, J. L., et al., Eds., Ch.7, p.131-146 (1989); and Rae, P., and DiLullo, G., SPE Paper No. 37359 (1996)]. In accordance with this application vasospasm(s) agent(s), which is suitable for use in the described compositions and methods of treatment of underground formations, can be an organic or inorganic peroxide, both of which can be either water soluble or only weakly soluble in water. Used in this application, the term "organic peroxide" refers to organic peroxides (compounds containing the link of the oxygen-oxygen (-O-O-) (proxygroup)), and organic hydroperoxides, and the term "organic peroxide" refers to inorganic compounds containing the element in the higher oxidation state (such as HClO4or containing a peroxide group (--O-O--). The term "slightly soluble"used in relation to thinning agents, refers to the solubility of the organic peroxide or an inorganic peroxide in water, equal to about 1 g/100 g of water or less at room temperature and normal pressure. Preferably, the solubility of the peroxide was equal to about 0.10 g or less in 100 g of water. The solubility of the peroxide used as a thinning agent invented the Yu, can be determined using any suitable method, including without limitation, method, HPLC, volumetrically methods and methods of titration, for example iodometric titration described in Vogel''s Textbook of Quantitative Chemical Analysis, 6thEd., Prentice Hall, (2000). In accordance with this aspect of the invention provides methods for delivering fluid to the well treatment (such as liquid gap), including polysaccharide, slightly soluble borate crosslinking agent and modifier staple in the underground formation, which passes the wellbore, contacted stable borate crosslinked fluid with organic or inorganic-thinning agent, which is soluble or only slightly soluble, while thinning agent is contained in an amount which is sufficient to reduce the viscosity. In accordance with such methods could be used to periodically process the individual parts of cross-linked organic or inorganic liquids-thinning agent, which is periodically fed into the borehole, or you can handle all sewn fluid used to carry out this operation when the thinning agent is continuously fed into the well. Organic peroxides suitable for use as a thinning agent in accordance with this invention can have high energy asset the AI for the formation of peroxide radicals and relatively high storage temperature, which usually amount to about 80°F. High activation energy and temperature of storage of organic peroxides give stability to the compositions, which in turn leads to an acceptable term viability. Preferred organic peroxides suitable for use as thinning agents include, without limitation, Gidropress cumene, trebuil-Gidropress, peroxide trebuil-hydroperoxide, di-trebutaries, di-(2-trebotivishta)benzene, 2,5-dimethyl-2,5-di-(trebutaries)hexane, monohydroperoxide di-isopropylbenzene, dicumylperoxide, 2,2-di-(trebutaries)butane, tretiakovskii, benzoyl peroxide, mixtures thereof and mixtures of organic peroxides with one or more additional agents, such as potassium persulfate, nitrogen-containing ligands (e.g., EDTA or 1,10-phenanthrolin). For example, Gidropress cumene has a low solubility in water, equal to about 0.07 g/100 g of water, the activation energy is approximately 121 kJ mol in toluene, and the half-life of approximately 10 hours at a temperature of 318°F. For use according to the invention preferred a slightly water-soluble inorganic and organic peroxides, as they are better kept in the gap during injection than water-soluble inorganic or organic peroxide. Not limiting the Yas by any one theory, the reason for this see what retention, probably due to the presence of the precipitate the polysaccharide. This precipitate, when it is affected by the differential pressure during injection into an underground formation that allows the aqueous phase to pass through its thickness. After passing through the sediment water and any related water-soluble substances can come in a matrix formation. Accordingly, water-soluble peroxide can act like persulfates with the faction, decaying in a matrix formation. In contrast, most of the slightly water-soluble inorganic and organic peroxides, proposed for use according to the invention, are not in the aqueous phase and, consequently, do not pass through the residue of the polysaccharide in the formation. Most inorganic and organic peroxides described above and suitable for introduction into the liquid according to the invention can be captured sediment. Therefore, the concentration of inorganic and organic peroxides will increase in the gap is almost the same speed as the concentration of polysaccharide held amount sufficient to decompose as liquids and sludge. The rate of decomposition of the slightly water-soluble inorganic and organic peroxides depends both on temperature and on the concentration of inorganic or organic the Russian peroxide. The number used slightly water-soluble organic peroxides should be sufficient to reduce the viscosity or the destruction of the gel without premature reduce the viscosity. For example, if a gel-like polysaccharide has a molecular weight of about two million and the desired reduction in molecular weight of approximately 200,000 or less, then the reduction will lead to the formation of about ten segments of the polymer. The concentration of the organic peroxide equal to 20 hours/million, will lead to degradation of the polysaccharide without premature reduce the viscosity. Preferably, the amount of organic peroxide was in the range of from about 5 o'clock/m to about 15000 hours/million per liquid. Typically, the concentration depends on the content of the polysaccharide, preferably from about 0.24% to about 0,72% (wt./vol.), and on temperature. Used temperature in the case of these peroxides are in the range from about 125°F to about 275°F, and the pH can range from about 3 to about 11. In addition, the average particle size of peroxide-thinning agent may be equal to from about 20 mesh to about 200 mesh, and more preferably from about 60 mesh to about 180 mesh. Inorganic peroxide, suitable as thinning agents in the compositions according to the invention, include, without limitation, alkaline peroxide m is the metal, the alkaline earth metal peroxide, peroxides of transition metals and combinations thereof, such as described Skiner, N. and Eul, W., in Kirk-Othmer Encyclopedia of Chemical Technology, J. Wiley & Sons, Inc., (2001). Examples of suitable peroxides of alkali metals include, but are not limited to, sodium peroxide, sodium hypochlorite, potassium peroxide, potassium persulfate, potassium superoxide, peroxide lithium, and mixtures of these peroxides such as sodium peroxide/potassium. Examples of alkaline earth metal peroxides include hydrogen peroxide of magnesium, calcium peroxide, strontium peroxide and barium peroxide, and mixed peroxides, such as peroxide calcium/magnesium. Peroxide transition metals, which can be used in the compositions described in this application include any peroxide containing a metal of groups 4 to 12 of the Periodic table of elements, such as peroxide zinc. Additional additives that may be used is described in liquids for treatment of wells, can be stabilizers of enzyme-thinning agents (proteins). These compounds can stabilize any enzyme and/or protein used in liquids for processing in order to "break" the gel after treated subterranean formation, so that they remain effective when it is desirable to destroy the gel. If the enzymes decompose too early, they are not the Udut available for the effective destruction of the gel at the appropriate time. Non-limiting examples of stabilizers enzymes, which can be introduced into the fluid for the well treatment according to the invention include sorbitol, lures, glycerol, citrate, aminocarbonyl acids and their salts (EDTA, DTPA, NTA, and so on), phosphonates, sulfonates, and mixtures thereof. Retarding crosslinking additives and liquids for processing according to the invention can be used in the implementation of the treatment of underground formations where the need for such a fluid, such as intensification of wells or at the completion of the wells, and when the viscosity and crosslinking the liquid for treatment will be monitored and modified. Examples of processing operations underground formations include, without limitation, drilling of the wellbore, the completion of wells, the intensification of the underground formation by means of processing operations, such as gap (including hydraulic fracturing foam and/or acid treatment of wells (including structural acid treatment and acid gap), the deviation, the fight against ingress of water, fighting the flow of sand (such as gravel backfill), and numerous other operations treatment of underground formations, preferably those associated with extraction operations liquefied hydrocarbons. Used in this application, the term "treatment" refers to any activity under the earth, in which the use is conducted liquid with a desired function and/or for the desired purpose. The term "treatment" does not imply any particular action of liquids according to this invention. Other options for applying one or more aspects of the inventions described above can be developed, without going beyond the scope of this invention. In addition, various methods and options liquids for well treatment and application described in this application can be included in combination with each other with getting variations of the described methods, compositions and applications. The discussion of individual items may include many elements, and Vice versa. The following examples are included to demonstrate preferred variants of the invention. Specialists in this field it is obvious that the techniques described in the examples represent preferred methods for carrying out the present invention. But experts it is clear that, given this description, you can implement many of the changes described specific options and still obtain a like or similar result without going beyond the limits and scope of the invention. Examples Example 1. A common method of assessing the degree of crosslinking The degree of crosslinking of several boron-containing ores was determined using standard methods, as described, for example, in U.S. patent No. 7018956. In General, for carrying out the crosslinking was prepared 2% solution gua is and by dissolving 5 g of potassium chloride (KCl) in 250 ml of distilled or tap water and then adding 7 g of the guar resin, such as WG-35™ (available from Halliburton Energy Services Inc., Duncan, OK) or its equivalent. The resulting mixture was stirred verhneprivodnaya agitator within 30-60 min for holding hydration. As soon as guar gum was gidratirovana completely determined the pH of the solution using the standard sample and recorded the temperature. Usually the initial mixture of the guar resin has a pH ranging from about 7.5 to about 8.0 and the initial viscosity (defined using the FANN viscometer®Model 35A, Fann Instrument Company, Houston, TX)equal to from about 16 SP to about 18 SP at a temperature of 77°F. 250 ml solution of guar was placed in a clean, dry blender of Moringa and the motor speed blender regulated by a rheostat (for example, voltage regulator Variac) to obtain a vortex in the solution Guara so that the cap nut (bolt the blades of the blender) and a small surface of the blade, which surrounds the cap nut on the bottom of the blender were free from liquid, but not at such a height, in order to capture a significant amount of air in solution Guara. While maintaining a specified speed was added to 0.44 ml of a solution of a crosslinking additive containing slightly soluble borate, to effect the crosslinking of the mixture containing guar polymer. After adding just a sample of boron-containing material to a solution of guar poly the EPA included a timer. The rate of fusion was expressed in three different entry points in time: the stop time vortex. T1the beginning of the static mixing T2and the moment of appearance of the hanging edge, T3. T1is defined as the time that has elapsed between the time when he was added to the stapler/boron-containing material, and the time when the cap nut in the blender was completely closed fluid. T2was defined as the time that has elapsed between the time of adding the stapler/boron-containing material and the moment when the upper surface of the liquid in the blender stops to rotate/move and becomes static. These two measured values are indicated in the tables as VC ("stopping vortex") and ST ("static mixing"), respectively. The rate of mixing in a blender remained constant during this experience (although the actual speed of mixing can be reduced by increasing the viscosity of the crosslinked fluid). After recording the values of T2mixing was stopped and the liquid was stirred manually in two cups to monitor the consistency of the crosslinked composition. The third measured value (T3it was the moment hangs in the region, this is the time that passed between when it was added crosslinking agent, and when cross-linked liquid forms a hard edge, which which hangs from the edge of the glass. Specialists in this field can use these parameters, although some techniques may differ from those described above. Example 2. Comparison of time staple in the liquid water-based and liquid oil-based Concentrates for crosslinking were prepared in an environment of water and diesel oil known methods. In particular, water-based concentrate was obtained by mixing 2 g attapulgite clay (FLORIGEL®HY, Floridan Company, Quincy, FL), 0,857 g low-viscosity polyanionic cellulose (GABROIL®LV, Akzo Nobel, The Netherlands), 0,957 ml of NALCO®9762 (viscosity modifier / deflocculant, Nalco Company, Sugarland, TX) and 49,97 g ground (D50=11 or 36) of ulexite from the area of Bigadic in Turkey in 72,82 ml of tap water Houston, TX. Concentrate on the basis of diesel oil was obtained by mixing and 2.14 g of a suspending agent, such as CLAYTONE®AF or TIXOGEL®MP-100 (Southern Clay Products, Inc., Gonzales, TX), 1.31 ml of emulsifier, such as Witco A (Chemtura Corp., Middlebury, CT) and 49,97 g chopped (D50≈11 or 36) of ulexite from the area of Bigadic in Turkey in 72,36 ml of diesel oil. 2%of a mixture of KCl and the guar resin used in water-based concentrate, and concentrate-based diesel oil, was obtained as a model of a typical fluid processing formations; it contained a mixture of 5 g of KCl and 0.7 g of the guar gums (WG-35™, Halliburton Energy services, Inc., Duncan, OK) in 250 ml of tap water from Houston, TX. Then the pH value of the mixture was set equal to 7 using dilute acetic acid (CH3C2H). The concentrate containing of 0.44 ml water-based or solution-based oil with suspended slightly soluble borate, mixed with 250 ml of a solution of the guar resin and determined the time of fusion at 100°F (37,78°C). The results of this comparison are shown in Table A. Table A shows that the distribution of particles with a high content of fine particles suspended in a saturated borate water has little effect on the time of crosslinking in the composition of the guar resin with a low pH. Changing the size of the D50particles of Borat from 11 to 26 MC changes the time of stitching only 3-5%, while the same substances in the concentrate oil-based changes the time of stitching 22%.
Example 3. Comparison of time-linkage for cross-linking additives potassium acetate/potassium carbonate Was prepared several compositions crosslinking additives containing different amounts of modifiers stitching potassium acetate (KC2H3O2) and potassium carbonate (K2CO3), and estimates the time of stapling. 2%of a mixture of KCl-guar gum was prepared as described above. Separately prepared 100 ml of a solution of a crosslinking additive with respect to an aqueous solution of CA2H3About2K2CO3specified in Tables B-E below. For example, in the preparation of the solution 93,76% vol. KC2H3O2/ 6,24% vol. To2CO3(Table B) 68,29 ml 10,22 pounds per gallon of potassium acetate solution (NA-CHURS/ALPINE Solutions, Marion, OH) was added to 4,54 ml solution of 11.75 lb/Gal potassium carbonate (NA-CHURS/ALPINE Solutions, Marion, OH) and the mixture was stirred for thorough mixing. To this solution KC2H3O2/K2CO3added 2 g attapulgite clay (FLORIGEL®HY, Floridan Company, Quincy, FL) and the solution was stirred in the mixer Hamilton Beach for about 15 minutes Then added 0,857 g low is askoy polyanionic cellulose (GABROIL ®LV, Akzo Nobel, The Netherlands) and was stirred solution for 15 minutes To this mixture was added 0,857 ml viscosity modifier/deflocculant NALCO®9762 (Nalco Company, Sugarland, TX) and 49,97 g finely ground (D50≈36) ulexite from the area of Bigadic in Turkey. 44 ml of a crosslinking additive CA2H3About2/ K2CO3with suspended slightly soluble borate was then mixed with 250 ml of a solution of the guar resin and determined the time of fusion at 100°F (37,78°C). The results of this comparison are shown in Tables B, C, D, and E below. Example 4. Comparison of time-linkage in the case of cross-linking additives potassium formate/carbonate potassium Was prepared several compositions crosslinking additives containing various amounts of modifiers stitching - potassium formate (KCO2H) and potassium carbonate (K2CO3) and determined the time of stapling with their application. A mixture of 2% KCl-the guar resin with a pH equal to 7, was prepared as described above. Separately prepared solution (100 ml) crosslinking additive with respect to an aqueous solution KCO2H to a solution of K2CO3listed below in Table F-I. for Example, when receiving a mixture of 2 according to Table F 67,31 ml of potassium formate (KCO2H, NA-CHURS/ALPINE Solutions, Marion, OH) with the end of the filtration 11,22 f/Gal. mixed with 5,06 ml of tap water Houston, TX, receiving the mixture with a concentration of 11.0 lb/Gal. To this mixture was added 0,457 ml of a solution of potassium carbonate (K2CO3, NA-CHURS/ALPINE Solutions, Marion, OH) (11,75 f/Gal.) and stirred the mixture to obtain a thoroughly mixed solution. To this solution KCO2H/K2CO3added 2 g attapulgite clay (FLORIGEL®HY, Floridan Company, Quincy, FL). Stirred the resulting solution using a mixer Hamilton Beach for about 15 minutes Then added 0,857 g low-viscosity polyanionic cellulose (GABROIL®LV available at Akzo Nobel, The Netherlands) and was stirred solution of 15 minutes To this mixture was added 0,857 ml viscosity modifier/deflocculant NALCO®9762 (available from Nalco Company, Sugarland, TX) and 49,97 g finely ground (D50≈36) ulexite from the area of Bigadic in Turkey. The pH value of the obtained cross-linking additives was equal 10,71. the pH of the solution the guar resin, described above, was set equal to 7 using dilute formic acid (HCO2H). Then of 0.44 ml of a crosslinking additive KCO2H/K2CO3with suspended slightly soluble borate was mixed with 250 ml of a solution of the guar resin and determined the time of crosslinking at a temperature of 100°F (37,78°C). The results are shown below in Tables F, G, H and I. Example 5. Comparing the time of stapling when using Stivali the additives, containing the acetate, chloride, acetate/acetic acid and slightly soluble borate without small particles/acetate Was prepared several compositions crosslinking additives containing different modifiers, and determined the time of stapling with their application. In particular, it was obtained a mixture containing potassium acetate, potassium chloride, potassium acetate with a pH set equal to 7.5 using acetic acid and potassium acetate in a mixture with slightly soluble borate particles larger than 325 mesh; set time stitching with their application method described later. First preparing a solution of guar resin by mixing 250 ml of tap water Houston, TX, 5 g of potassium chloride (KCl, available at Univar USA, Inc., Houston, TX) and 0.7 g of the guar gums (WG-35™, available at Halliburton Energy Services, Inc., Duncan, OK). This solution of the guar resin had an initial viscosity of 16 CPS (at 77°F (25°C), measured using a viscometer FANN Model 35A (Fann Instrument Company, Houston, TX). The pH value of the mixture containing guar gum, was set equal to 7 using dilute acetic acid (CH3CO2H). The solution of crosslinking additives KC2H3O2(62,29 wt.%) was prepared by mixing 72,83 ml KC2H3O2(10,22 f/Gal.) and 2 g attapulgite clay (FLORIGEL HY, available in Floridan Company, Quincy, FL). The solution was stirred in the mixer Hamilton Beach for about 15 minutes Then added 0,857 g low the viscous polyanionic cellulose (GABROIL ®LV available at Akzo Nobel, The Netherlands) and the solution was stirred for another 15 minutes To this mixture was added 0,857 ml viscosity modifier/deflocculant NALCO®9762 (available from Nalco Company, Sugarland, TX) and 49,97 g finely ground (D50≈36 or D-50≈36, sieve 325 mesh) of ulexite from the area of Bigadic in Turkey. Then prepared KCl solution by mixing 98,7 g HCl (Univar USA, Inc., Houston, TX) with 308,35 ml of tap water Houston, TX. The solution was mixed and filtered through a paper filter, Shark Skin, the filtrate was a saturated solution of KCl. Then got the solution using 72,83 ml KCl (9,7 f/Gal.), 2 g attapulgite clay (FLORIGEL®HY, Floridan Company, Quincy, FL), 0,857 g low-viscosity polyanionic cellulose (GABROIL®LV available at Akzo Nobel, The Netherlands), 0,857 ml viscosity modifier/deflocculant NALCO®9762 (Nalco Company, Sugarland, TX) and 49,97 g finely ground (D50≈36) ulexite, as described earlier. Received the solution 61,46% wt. KC2H3O2/ 0.84 wt.% CH3CO2H (crosslinking additive) by mixing 71,69 ml KC2H3O2concentration 10,22 f/Gal., 1,14 ml CH3CO2H with a concentration of 8.75 lb/Gal 2 g attapulgite clay (FLORIGEL®HY, Floridan Company, Quincy, FL), the resulting solution was Stirred using a mixer Hamilton Beach for about 15 minutes Then added 0,857 g low-viscosity polyanionic cellulose (GABROIL ®LV available at Akzo Nobel, The Netherlands) and was stirred solution of 15 minutes To this mixture was added 0,857 ml viscosity modifier / deflocculant NALCO® 9762 (available from Nalco Company, Sugarland, TX) and 49,97 g finely ground (D50≈36) ulexite from the area of Bigadic in Turkey. Then of 0.44 ml concentrate KC2H3O2/ CH3CO2H with suspended slightly soluble borate was mixed with 250 ml of a solution of the guar resin and determined the time of crosslinking at a temperature of 100°F (37,78°C). The results of these experiments are shown in Table J. Example 6. A comparison of time-linkage using alkaline potassium acetate and potassium formate in cross-linking additives There were prepared compositions crosslinking additives containing different amounts of modifiers stitching potassium acetate (KC2H3O2) and potassium formate (KCO2H), and estimated time staple in the solution of the guar resin. Preparing a solution of guar resin with a pH of 7, as described above, by using the resin WG-35™ (Halliburton Energy Services, Inc., Duncan, OK), with an initial viscosity 16-18 JV, determined at a temperature of 77°F (25°C) when the rotation speed of 300 rpm on a FANN viscometer®Model 35A. Were obtained solutions of cross-linking additives KC2H3O2and KCO2H at the concentrations shown in Tables K and L, according to the methods described in this application. For example, what was alocale 100 ml of a crosslinking additive 60,58% wt. KC 2H3O2/ 1,87% K2CO3(Table K) by mixing 71 ml KC2H3O2(10,22 f/Gal.), 1,83 ml K2CO3(11,75 f/Gal.) and 2 g attapulgite clay (FLORIGEL®HY, Floridan Company, Quincy, FL). Stirred the resulting solution using a mixer Hamilton Beach for about 15 minutes Then added 0,857 g low-viscosity polyanionic cellulose (GABROIL®LV available at Akzo Nobel, The Netherlands) and was stirred solution of 15 minutes To this mixture was added 0,857 ml viscosity modifier / deflocculant NALCO®9762 (available from Nalco Company, Sugarland, TX) and 49,97 g finely ground (D50≈36) ulexite from the area of Bigadic in Turkey. The mixture of crosslinking additives had a pH value of 10,99. Other compositions described in Tables K and L, were obtained by the same method with the changes regarding the amounts of reagents depending on the final composition of a crosslinking additive, which should be tested. Then of 0.44 ml concentrate KC2H3O2and KCO2H with suspended slightly soluble borate was mixed with 250 ml of a solution of the guar resin and determined the time of crosslinking at a temperature of 100°F (37,78°C). The results of these experiments are shown in Table K and L. Observations based on the application of the solution of the guar resin with a low pH (pH 7.0) <> The results obtained in examples 3-6, when they studied the influence of the number of modifiers stitching (for example, a salt, an alkaline agent or an acidic agent) in accordance with this invention, the speed/time of crosslinking of the guar solutions of the resin at low pH (for example, around 7.0), show the ability of the described compositions to cause a strong change of time staple in liquids for treatment of wells without changing the properties of the crosslinked system. For example, Table C and G show that the addition of salts such as potassium acetate or potassium formate or potassium formate in the composition of a crosslinking additive for water-based reduces time staple of 65.1% and 49.6%, respectively. In addition, table C also shows that the presence of a solution of the modifier stitching, salt/alkaline agent (for example, 97,49% vol. KC2H3O2(8,90 f/Gal.) / of 2.51% vol. K2CO3(11,75 f/Gal.) in the composition of a crosslinking additive changes the time of stapling approximately 66.9 per cent, and the final pH value custom made system changes by only 0.1%. Similarly, table G shows that the presence of 97,49% vol. KCO3H (11 lb/Gal.) / of 2.51% vol. K2CO3(11,75 f/Gal.) in the composition of a crosslinking additive changes the time of stapling approximately 53.3%, and the target value of the pH of the crosslinked system remains unchanged.Tables B and F illustrate several additional important features of the invention when using the AI solutions of the guar resin with a low pH. For example, from the Table it is seen that with increasing number of K2CO3to about 0.47 wt.% in potassium acetate, time of crosslinking increases, but when the number of K2CO3becomes equal to more than about 0.47 wt.%, time stitching is reduced. Table F it is clear that increasing the number of K2CO3in the cross-linking additive, potassium formate, time stitching is reduced. Finally, Table B and F clearly show that the addition of salt and the alkaline reagent can reduce the time of stapling up to about 35, even though borate agent has a particle size D50 equal to 36 MK. The data in Table J illustrate some observations concerning the present invention. For example, you can see that when salt is added to the composition is water-based, containing slightly soluble borate and then the composition is mixed with a solution of the guar resin, the time of crosslinking decreases. However, adding an acidic reagent in a mixture containing salt, will increase the time of stapling. The use of large particles Borat without small particles can also increase the time stitching all studied compositions. Finally, table J shows that in accordance with this invention the salt that is different from the acetate and formate can be used to change the time stitching with the same favorable result. Table CI L also show other alkaline compounds (e.g., potassium hydroxide), mixed solutions of KC2H3O2and KCO2H, can be used to speed up the fusion process in solutions of the guar resin with a low pH. For example, solutions modifier staple containing 97,49% vol. KC2H3O2(8,90 f/Gal.) / of 2.51% vol. KOHN (9,06 f/Gal.) and 97,49% vol. KCO2H (11 lb/Gal.) / of 2.51% vol. KOH (9,06 f/Gal.) in the composition of a crosslinking additive may change the time of crosslinking on 72,9% and 60.7%, respectively, compared to a system made of a crosslinking additive is water-based. Example 7. Evaluation of the effect of increasing amounts of acetic acid and formic acid cross-linking additives, potassium acetate and potassium formate Received a number of compositions crosslinking additives containing various amounts of modifiers stitching, potassium acetate (KC2H3O2) / acetic acid (CH3CO2H) and potassium formate (KCO2H) / formic acid (HCO2H), determined the time of stapling when used in solutions HPG. The solution hydroxypropranolol resin (HPG) was prepared by mixing 0.96 g HPG (GW-32™, available at BJ Services, Tomball, TX) in 200 ml of tap water Houston, TX. The HPG solution had an initial viscosity, measured in a viscometer FANN®Model 35A when the rotation speed of 300 rpm, equal 29-33 JV at a temperature of 77°F, pH, Rav is the first 8,0-8,4, to establish a pH of 11.6, using diluted NaOH. Cross-linking additives KC2H3O2/CH3CO2H and KCO2H/HCO2H were obtained as described in this application, by mixing the required quantities of solutions KC2H3O2(10,22 f/Gal.) or KCO2H (11 lb/Gal.) with the 0-1,97 wt.% acetic acid or formic acid, attapulgite clay (FLORIGEL®HY, available in Floridan Company, Quincy, FL), low viscosity polyanionic cellulose (GABROIL®LV available at Akzo Nobel, The Netherlands), viscosity modifier/deflocculant NALCO®9762 (available from Nalco Company, Sugarland, TX) and very fine (D50≈11) of ulexite from the area of Bigadic, Turkey. 0,50 ml additives KC2H3O2/CH3CO2H and KCO2H/HCO2H with suspended slightly soluble borate was mixed with 200 ml HPG and determined the time of crosslinking at a temperature of 80°F (26,67°C). The results of these experiments are shown in Tables M and N below. Example 8. Comparison of the results obtained in the presence of crosslinking additives of potassium acetate and potassium formate and acidic agents Received a number of compositions crosslinking additives containing different amounts of modifiers stitching, potassium acetate (KC2H3O2) and potassium formate (KC2H3O2and acid is, then determined time staple in the HPG solutions. The HPG solution was prepared as described in example 7, using GW-32™ (available from BJ Services, Tomball, TX), the initial viscosity of the solution, measured at a speed of 300 rpm at a temperature of 77°CF (25°C) using a viscometer FANN® Model 35A, was equal 29-33 SP, the initial pH value was equal to 8.0-8.4 to bring this value up to 11.6 using diluted NaOH. Solutions of cross-linking additives KC2H3O2and KCO2H were obtained with concentrations listed in Tables O and P. for Example, 100 ml of a crosslinking additive - 60,30% wt. KC2H3O2/ 1.97 wt.% HCl (table A) was obtained by mixing of 70.4 ml KC2H3O2(10,22 f/Gal.), 2,43 ml HCl (9,83 f/Gal.) and 2 g attapulgite clay (FLORIGEL®HY, available in Floridan Company, Quincy, FL). Then this solution permisible in the mixer Hamilton Beach for about 15 minutes Then added 0,857 g low-viscosity polyanionic cellulose (GABROIL®LV available at Akzo Nobel, The Netherlands) and the solution was stirred for another 15 minutes To this mixture was added 0,857 ml viscosity modifier/deflocculant NALCO®9762 (available from Nalco Company, Sugarland, TX) and 49,97 g finely ground (D50≈11) of ulexite from the area of Bigadic in Turkey. The pH of the mixture was approximately 8,04. Other compositions described in Tables O and P were prepared in a similar method, but with the change in the number of the reagents (for example, HCl, CH3CO2H or HCO2H) depending on the final composition of a crosslinking additive. 50 ml KC2H3O2and KCO2H with suspended slightly soluble borate was mixed with 200 ml HPG and determined the time of crosslinking at a temperature of 80°F (26,67°C). The results of these experiments are shown in Tables O and P. Example 9. The effect of increasing the amount of potassium carbonate or acetic acid crosslinking additive, potassium acetate Was prepared several compositions crosslinking additives containing modifiers stitching potassium acetate (KC2H3O2) and various amounts of potassium carbonate (K2CO3) or acetic acid (CH3CO2H) and then determined the time of stapling in solutions HPG. The HPG solution (hydroxypropylcellulose resin) was obtained as described in example 7, using GW-32™ (available from BJ Services, Tomball, Texas), the initial viscosity, measured using a FANN viscometer®Model 35A at a temperature of 77°F (25°C) and a speed of 300 rpm, was equal 29-33 SP, the initial pH value was equal to 8.0-8.4 to bring this value up to 11.6 using diluted NaOH. Solutions of cross-linking additives KC2H3O2prepared with concentrations listed in Tables Q and R, the methods described in this application. For example, 100 ml of a crosslinking add the and, consisting of 61,28% wt. KC2H3O2/ 0.88 wt.% CH3CO2H (table R), was obtained by mixing 71,54 ml KC2H3O2(10,22 f/Gal.), of 1.29 ml CH3CO2H (8,75 f/Gal.) and 2 g attapulgite clay (FLORIGEL®HY, Floridan Company, Quincy, FL). The solution was stirred in the mixer Hamilton Beach for about 15 minutes Then added 0,857 g low-viscosity polyanionic cellulose (GABROIL®LV available in Arzo Nobel, The Netherlands) and the solution was stirred for another 15 minutes To this mixture was added 0,857 ml viscosity modifier/deflocculant NALCO®9762 (available from Nalco Company, Sugarland, TX) and 49,97 g finely ground (D50≈11) of ulexite from the area of Bigadic in Turkey. The resulting mixture had a pH value of approximately 8,81. Other compositions described in Tables Q and R, received a similar method, but changing the amounts of reactants (e.g., K2CO3or CH3CO2H) depending on the final composition of a crosslinking additive, which should be tested. 0,50 ml cross-linking additives KC2H3O2/ K2CO3or KC2H3O2/ CH3CO2H with suspended slightly soluble borate was then mixed with 200 ml HPG (hydroxypropranolol resin) and determined the time of crosslinking at a temperature of 80°F (26,67°C). The results of these experiments are shown in Tables Q and R. Example 10. The results obtained with increasing particle size in the cross-linking additives potassium acetate/potassium carbonate Received a number of compositions crosslinking additives containing modifiers fusion process is potassium acetate (KC2H3O2) and various amounts of potassium carbonate (K2CO3and slightly soluble borates with a large distribution of particle sizes, and estimated time staple in solutions HPG (hydroxypropranolol resin). The HPG solution (hydroxypropylcellulose resin) was obtained as described in example 7, using GW-32™ (available from BJ Services, Tomball, Texas), the initial viscosity, measured using a FANN viscometer®Model 35A at a temperature of 77°F (25°C) and a speed of 300 rpm, was equal 29-33 SP, the initial pH value was equal to 8.0-8.4 to bring this value up to 11.6 using diluted NaOH. Were obtained crosslinking additives KC2H3O2/ K2CO3at the concentrations specified in Table S, the method described in this application. For example, 100 ml of a crosslinking additive consisting of 58,0% wt. KC2H3O2/ of 4.44 wt.% K2CO3(Table S), was obtained by mixing 68,29 ml KC2H3O2(10,22 f/Gal.), of 4.54 ml K2CO3(11,75 f/Gal.) and 2 g attapulgite clay (FLORIGEL®HY, Floridan Company, Quincy, FL). The solution is PE is masively in the mixer Hamilton Beach for about 15 minutes Then added 0,857 g low-viscosity polyanionic cellulose (GABROIL®LV available in Arzo Nobel, The Netherlands) and the solution was stirred for another 15 minutes To this mixture was added 0,857 ml viscosity modifier/deflocculant NALCO®9762 (available from Nalco Company, Sugarland, TX) and 49,97 g finely ground (D50≈36) ulexite from the area of Bigadic in Turkey. The pH of the mixture was equal 11,35. Other compositions described in Table S, were obtained in a similar way, but with a change of the quantities of reagents (e.g., KC2H3O2or K2CO3depending on the final composition of a crosslinking additive, the test which should be performed. 0,50 ml cross-linking additives KC2H3O2/ K2CO3with suspended slightly soluble borate was then mixed with 200 ml HPG and determined the time of crosslinking at a temperature of 80°F (26,67°C). The results of these experiments are shown below in Table S. Observations based on experiments with a high pH value (pH 1.1,6) solution HPG The results of examples 7 to 10, described above, in which was studied the influence of the number of modifiers stitching (for example, salts of alkaline or acidic agents) on the speed/time staple in the HPG solutions in accordance with this invention. At high values of pH (around 11.6) the composition described in the application is Oh, able to significantly change the time of stapling liquids for treatment of wells without changing the properties of the crosslinked system. Tables M and N show that at high pH values, for example at a pH of 11.6, time stitching solutions HPG exceed 12 min using very small particles in the cross-linking additives, water-based. These tables also show that the addition of salts, such as potassium formate in the composition of a crosslinking additive for water-based reduces time staple for more than 30%, and add salt and acid in the composition of a crosslinking additive reduces the amount of time stitching more than 80% (compared with the composition water-based), below 1:45. In addition, table M shows that the presence of a solution of the modifier stitching 96,67% vol. KC2H3O2(10,22 f/Gal.) / 3,33% vol. CH3CO2H (8,75 f/Gal.) in the composition of a crosslinking additive changes the time stitching on 86,4%, while the target value of the pH of the crosslinked system varies only by 5.4%. Similarly, table N shows that the presence of a solution of the modifier staple in the number 96,67% vol. KCO2H (11 lb/Gal.) / 3,33% vol. HCO2H (10,16 f/Gal.) in the composition of a crosslinking additive changes the time stitching on 89,6%, while the final pH value custom made system changes by only 3%. A comparison of time staple in Tables O and P shows that acid that is different from the UKS is Noah and formic (for example, salt), can be applied to accelerate the fusion process HPG water-based systems. For example, the introduction of solutions modifiers staple in the number 96,67% vol. KC2H3O2(10,22 f/Gal.) / 3,33% vol. HCl (9,83 f/Gal.) and 96,67% vol. KCO2H (11 lb/Gal.) / 3,33% vol. HCl (9,83 f/Gal.) in the composition of a crosslinking additive may change the amount of time staple for more than 80% compared to a system made of a crosslinking additive is water-based. Tables Q and R show that the increase in the number of modifiers stapling K2CO3and CH3CO2H with decreasing amounts KC2H3O2will progressively accelerate time staple in the HPG solutions at high pH values. The results of the experiments in Table S shows that, in contrast to the results in Table Q, the behavior of solutions HPG high pH is affected by the particle size slightly soluble borate crosslinking agent. As shown in paragraph 1 in Tables Q and S, the moment of termination of the vortex (VC) is extended 32.3% as the particle size D5011 MK 36 MK in the cross-linking additive is water-based. The order of the stages described in this application can be any, unless otherwise specified. The various stages described in the application, can be combined with other stages and/or be split into several stages. Similarly, the elements of the s have been described functionally and can be implemented as separate components or can be combined into components, having several functions. These inventions have been described in the context of the preferred and other alternatives, but described was not every variant of the invention. Specialists obvious modifications and changes to these options. Described and undescribed variants do not limit the scope or applicability of inventions created by the applicants, and in accordance with the patent laws, applicants intend to fully protect all such modifications and improvements within the scope of the invention defined by the claims and taking into account theory of equivalents. 1. Composition for reducing the time of crosslinking of aqueous solutions of stitched organic polymer, including: 2. The composition according to claim 1, in which the stitching viscous organic polymer is a polysaccharide. 3. The composition according to claim 2, in which the polysaccharide is guar, cellulose, starch, galactomannan resin, xanthan gum, actinopyga, or scleroglucan, or their derived. 4. The composition according to claim 3, in which the polysaccharide is selected from the group consisting of guar of hydroxypropanoate (HPG), carboxyphenoxypropane (CMHPG), methyl cellulose, hydroxyethyl cellulose (NES), hydroxypropylcellulose (LDCs), hydroxymethylcellulose, hydroxyethylmethylcellulose, hydroxypropylmethylcellulose, hydroxyethylmethylcellulose, methylhydroxyethylcellulose, methylhydroxypropylcellulose, metilgidroxiatilzelllozu, karboksimetilcelljulozy, carboxymethylcellulose or karboksimetiltselljulozy (SMNS). 5. The composition according to claim 1, in which the borate crosslinking agent is a borate, alkaline earth metal, mixed borate, alkaline earth metal - alkali metal or alkali metal borate containing two atoms of boron in the molecule. 6. The composition according to claim 5, in which the borate crosslinking agent selected from the group consisting of ulexite, colemanite, probertite and mixtures thereof. 7. The composition according to claim 1, in which the concentration of borate cross-linking agent is in the range from 0.1 kg/m3up to 5 kg/m . 8. The composition according to claim 7, in which the concentration of borate cross-linking agent is in the range from 0.25 kg/m3to 2.5 kg/m3. 9. The composition according to claim 1, in which the first modifier linkage selected from the group consisting of CSR2N and KC2H3O2and the second modifier linkage selected from the group consisting of CH3CO2N HCO2N, NaCO2H, NaC2H3O2, KCl, and KOH. 10. The composition according to claim 1, in which the modifier stitching is a reducer of the freezing point. 11. The composition according to claim 1, which further comprises suspendisse agent in an amount of 1 pound per barrel equals 42 gallons, up to 10 pounds per barrel equals 42 gallons. 12. The composition according to claim 11, in which suspendisse agent is palygorskite clay selected from the group consisting of attapulgite, sepiolite and mixtures thereof. 13. The composition according to claim 1, further containing an additive selected from the group consisting of buffers, permeability modifiers, additives that reduce water yield, biocides and corrosion inhibitors. 14. The composition according to claim 1, which represents a fluid for fracturing, in which the modifier stitching increases the speed at which the boron-containing crosslinking agent provides gelation stitched organic polymer at pH values higher than 8. 15. The composition according to 14 frac fluid, optionally containing proppant. 16. The method of treatment of underground formations, including: 17. The method according to clause 16, in which the borate crosslinking agent is a borate, alkaline earth metal, see shanny borate and alkaline earth metal alkali metal or alkali metal borate containing two atoms of boron in the molecule. 18. The method according to 17, which is slightly soluble borate selected from the group consisting of ulexite, colemanite, probertite and mixtures thereof. 19. The method according to clause 16, in which the first modifier linkage selected from the group consisting of KCO2H and KC2H3O2and the second modifier linkage selected from the group consisting of CH3CO2H, HCO2H, NaCO2H, NaC2H3O2, KCl, and KOH. 20. The method according to item 16, further including shipping in the underground formation peroxide inorganic or organic recepies. 21. The method according to claim 20, in which the inorganic peroxide or an organic rosepetal slightly soluble in water.
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