WO2013070728A1 - Système et procédé d'injection d'acide peracétique - Google Patents

Système et procédé d'injection d'acide peracétique Download PDF

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Publication number
WO2013070728A1
WO2013070728A1 PCT/US2012/063902 US2012063902W WO2013070728A1 WO 2013070728 A1 WO2013070728 A1 WO 2013070728A1 US 2012063902 W US2012063902 W US 2012063902W WO 2013070728 A1 WO2013070728 A1 WO 2013070728A1
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WO
WIPO (PCT)
Prior art keywords
paa
water
mixer
intake water
injection
Prior art date
Application number
PCT/US2012/063902
Other languages
English (en)
Inventor
Gred A. CONRAD
Original Assignee
Nch Corporation
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Nch Corporation filed Critical Nch Corporation
Publication of WO2013070728A1 publication Critical patent/WO2013070728A1/fr

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Classifications

    • C—CHEMISTRY; METALLURGY
    • C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K8/00—Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
    • C09K8/60—Compositions for stimulating production by acting on the underground formation
    • C09K8/62—Compositions for forming crevices or fractures
    • C09K8/72—Eroding chemicals, e.g. acids
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/40—Mixing liquids with liquids; Emulsifying
    • B01F23/45—Mixing liquids with liquids; Emulsifying using flow mixing
    • B01F23/451—Mixing liquids with liquids; Emulsifying using flow mixing by injecting one liquid into another
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/30—Injector mixers
    • B01F25/31—Injector mixers in conduits or tubes through which the main component flows
    • B01F25/313—Injector mixers in conduits or tubes through which the main component flows wherein additional components are introduced in the centre of the conduit
    • B01F25/3133—Injector mixers in conduits or tubes through which the main component flows wherein additional components are introduced in the centre of the conduit characterised by the specific design of the injector
    • B01F25/31331—Perforated, multi-opening, with a plurality of holes
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F33/00—Other mixers; Mixing plants; Combinations of mixers
    • B01F33/50—Movable or transportable mixing devices or plants
    • B01F33/502—Vehicle-mounted mixing devices
    • B01F33/5022—Vehicle-mounted mixing devices the vehicle being a carriage moving or driving along fixed or movable beams or bridges
    • C—CHEMISTRY; METALLURGY
    • C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B20/00—Use of materials as fillers for mortars, concrete or artificial stone according to more than one of groups C04B14/00 - C04B18/00 and characterised by shape or grain distribution; Treatment of materials according to more than one of the groups C04B14/00 - C04B18/00 specially adapted to enhance their filling properties in mortars, concrete or artificial stone; Expanding or defibrillating materials
    • C—CHEMISTRY; METALLURGY
    • C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K8/00—Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
    • C09K8/60—Compositions for stimulating production by acting on the underground formation
    • C09K8/62—Compositions for forming crevices or fractures
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F2025/91—Direction of flow or arrangement of feed and discharge openings
    • B01F2025/918—Counter current flow, i.e. flows moving in opposite direction and colliding

Definitions

  • This invention relates to a method and apparatus for injecting peracetic acid into various water supply sources as a clarifying agent to reduce or remove biological contaminants and to increase the pumpability so that the treated water can be used in oil-field operations, particularly in fracturing operations.
  • a fracturing fluid is sent down a well (typically a conventional horizontal well) under sufficient pressure to fracture the face of the mineral formation throughout the formation. Fracturing releases the hydrocarbon trapped within the formation and the hydrocarbon may then be extracted through the well. As the pressure on the face of the fractured mineral is released to allow for the extraction of the hydrocarbon fuel, the fracture in the formation would normally close again.
  • proppants such as course sand or sintered bauxite, are often added to the fracturing fluid to hold the fractures open, thereby increasing the effectiveness of the fracturing fluid. The fractures, held open by the proppants, form a channel through which the trapped hydrocarbons may escape after pressure is released.
  • Water from various sources is commonly used as the primary fluid in fracturing fluids.
  • the operations typically require large amounts of water, which may be supplied from nearby fresh water ponds, lakes and rivers.
  • produced water both ground water and recovered injected water
  • These water sources typically contain suspended solids, bacteria, or other organic or biological material, which may foul the formation.
  • suspended solids may clog the fractures, bacteria or other organic material that may grow within the formation, and scale may build-up, all of which interfere with the recovery of the natural gas. Additionally, these materials may interfere with the pumpabifity of the fracturing fluid, which must be pumped at high pressure to effectively create fractures in the formation.
  • fouling and pumpability problems may be compounded as each water source may have different types or levels of contaminants.
  • various additives are used with the fracturing fluid to address fouling problems. These include friction reducers, scale inhibitors, and water clarifiers/biocides.
  • peracetic acid also known as peroxyacetic acid or PAA
  • PAA peracetic acid
  • U.S. Patent Application Publication No. 2010/0160449 discloses a PAA composition and method using the PAA composition as a well treatment fluid by simply directing the fluid into a subterranean environment.
  • the ⁇ 56 patent application does not disclose any particular apparatus or methodology for effectively introducing the PAA into the well or the fracturing fluid.
  • the method and apparatus disclosed herein use PAA injection to effectively treat water from various sources to remove or reduce fouiing contaminants so that the treated water may be used as a fracturing fluid or otherwise used in oil and gas operations.
  • PAA is injected into the water supply line upstream of the frac tank (or on the intake side of the frac tank), thereby treating the water before introducing any other additives and before introducing the water to either the frac tank or the well.
  • an intake manifold is used to combine multiple sources of water prior to injecting the PAA for treatment. These embodiments have the advantage of allowing maximum time for treatment of the water, which minimizes damage to the formation when the treated water is used as a fracturing fluid.
  • an outlet manifold is used to direct the treated water to one or more frac tanks.
  • an injection quill is used to evenly disperse the PAA into the water in a mixer.
  • the configuration of the quill and mixer provide sufficient residence time to thoroughly mix the PAA and water (and begin treating the water) prior to discharge from the mixer. By thoroughly mixing the water with PAA, the water may be more efficiently clarified and treated for fracturing use. Because intake water may come from multiple sources, the volume and level of PAA needed to adequately treat the water will vary at different operation sites and may vary over time at a single operation site.
  • the apparatus of this embodiment is preferably designed so that the injection quill is interchangeable with differently sized and configured quills to permit varying PAA flow rates into the mixer. This permits flexibility in operation to increase or decrease the rate of injection so that the water is effectively treated without use of excess chemicals.
  • a method for injecting PAA into intake water from one or more sources and discharging the treated water to one or more frac tanks is disclosed.
  • the PAA is injected evenly across a mixer with the direction of PAA flow directed substantially opposite the direction of flow of the intake water to aid in thoroughly mixing the PAA and intake water.
  • methods for testing the PAA level are provided. Because of the varying levels of fouling agents in different water sources, the PAA demand needs to be determined at the beginning of the process and periodically monitored as the water is being treated by injection of PAA using testing methodologies that include sampling and dosing to determine the amount of PAA to be added to achieve PAA concentrations of 20-60 ppm. Based on the results of these testing methods, the amount of PAA being injected can then be adjusted as necessary throughout the process. This ensures that an adequate amount is used to achieve the desired level of treatment without using more PAA than necessary, which is wasteful and costly and may damage the formation.
  • FIG. 1 is a side elevation view of one embodiment of an apparatus according to the invention
  • FIG. 2 is a cross-sectional view of the PAA control valve and mixer assembly of the embodiment of FIG. 1 ;
  • FIG. 3 is a simplified process flow diagram illustrating principal parts of another embodiment of a multiple tank apparatus according to the invention.
  • FIG. 4 is a perspective view of a manifold assembly of an embodiment of the invention.
  • FIG. 5 is a cross-sectional view of a PAA control valve assembly of an embodiment of the invention.
  • FIG. 6 is a perspective view of a quill assembly of an embodiment of the invention.
  • FIG. 6B is a perspective view of a nozzle used in the quill assembly
  • FIG. 7 is a cross-sectional, exploded view of the quill assembly of FIG. 7;
  • FIG. 8 is a partially broken away cross-sectional view of a portion of the manifold assembly of FIG. 4;
  • FIG. 9 is a perspective view of an alternate embodiment of the manifold assembly of FIG. 4 mounted on a trailer;
  • FIG. 10 is a plan view of the embodiment of FIG. 9.
  • FIG. 11 is a front elevation of the embodiment of FIG. 9.
  • FIG. 1 one embodiment of a single tank apparatus 10 for injecting PAA is depicted.
  • Water from any source such as a pond or lake, is pumped to the location of single tank apparatus 10 through water supply line 18.
  • Water enters the PAA mixer and control valve assembly 20, where it is mixed with PAA pumped in from PAA supply tank 22 through PAA supply line 24.
  • Treated water exits the PAA mixer and control valve assembly 20 through treated water discharge line 32 and is stored in frac tank 38 until being pumped into a well as a fracturing fluid.
  • Other additives, such as friction reducers and scale inhibitors and proppants may be added to frac tank 38 using known methods.
  • connection fittings 60 and 62 connect water supply line 18 and treated water discharge line 32 to assembly 20.
  • Connection fittings 60 and 62 are standard fittings of any type suitable for connecting pipes or hoses together. The use of connection fittings 60 and 62 allow for easy installation of assembly 20 into existing configurations for supplying water to a frac tank, preferably on the water intake side.
  • connection fitting 62 may be attached directly to a corresponding fitting on the frac tank 38, allowing treated water to be discharged directly into the frac tank, however, discharge line 32 will typically be used to connect assembly 20 with frac tank 38 (as shown in FIG. 1 ).
  • a similar connection fitting 40 is providing to connect assembly 20 to PAA supply line 24.
  • a ball valve 42 having a handle 44, housing 46, and ball 48, controls the supply of PAA into assembly 20 through supply line 24.
  • ball valve 42 When ball valve 42 is open, PAA is allowed to flow into assembly 20 from a PAA supply tank (not shown).
  • ball 48 is preferably a vented ball, having a vent opening 50 that vents upstream when the valve 42 is closed.
  • check valve 52 is preferably a ball-type check valve, having a ball 56 and a spring 54 that cooperate to prevent water and PAA from flowing backward toward ball valve 42.
  • check valve 52 is configured so that PAA only flows through check valve 52 and into injection port 28 if sufficient pressure is supplied. PAA is then injected into mixer 58 through injection port 28 under sufficient pressure to thoroughly mix with water from water supply line 18.
  • Ball valve 42 and check valve 52 are standard type valves commonly used in chemical plants and oilfield operations. However, because of the high pressures at which PAA is injected into mixer 58, commercially available check valves may not have a spring 54 with the proper force constant. Accordingly, spring 54 may need to be custom built using methods and materials known to those of ordinary skill in the art. These valves 42 and 52 are connected together and to the PAA supply line 24 and injection port 28 using known connection methods, such as threaded connections or compression fittings. Once the PAA is thoroughly mixed with the water in mixer 58, it is discharged as treated water through discharge line 32.
  • injection port 28 and mixer 58 are made from stainless steel since they are directly in contact with high concentrations of PAA.
  • injection port 28 and mixer 58 may be made of virgin PTFE Teflon or other appropriately strong material.
  • Injection port 28 is preferably the 1 inch diameter size typically used for injection tubes in fracturing operations, although other sizes may be used.
  • Injection port 28 may be detachable from mixer 58 via any suitable connection means, such as a threaded connection.
  • injection port 28 may be permanently attached to or integrally formed with mixer 58.
  • Check valve 52 is preferably an atomizer type, such that PAA is atomized as it is introduced into mixer 58 through the injection port 28.
  • atomizer nozzles may be incorporated into injection port 28.
  • a fine spray dispersion of the PAA helps facilitate thorough mixing of the PAA and water inside mixer 58 before the water is discharged as treated water through discharge line 32.
  • the PAA is preferably injected into mixer 58 at around 300 psi to facilitate mixing.
  • mixer 58 is sized to provide sufficient residence time of the water and PAA within the mixer to achieve complete mixing; although it is not necessary that there be sufficient residence time to fully treat the water in the mixer, as the PAA will continue treating the water and acting as a biocide while being stored in frac tank 38.
  • Mixer 58 or discharge line 32 preferably have a standard sample port (not depicted) for obtaining samples of the treated water shortly after the PAA is injected in order to test the PAA level and make adjustments as described below.
  • a sample port or similar device may be used to allow visual inspection of the mixing quality at or near the treated water output. The PAA quality is measured by residual chemical after demand is met. If it appears that the PAA is not being thoroughly mixed with the intake water, then the PAA injection pressure may be adjusted to increase mixing.
  • FIG. 3 A simplified diagram of another preferred embodiment for a multiple tank apparatus 1 10 is shown in FIG. 3.
  • Apparatus 110 is similar to apparatus 10, except that it is configured to receive water from multiple water sources 1 12a-1 12d (such as ponds, lakes, or production water or from intermediate storage tanks holding water from such sources) and to discharge to multiple frac tanks 138a-138e. Water from all of the sources is pumped through water supply lines 1 14a-114d into inlet manifold 116 (which is preferably configured to receive water from at least four sources, but not all inlets on manifold 1 6 must be used and it may be configured for more than four water sources), where they are mixed together before being discharged through mixed water supply line 118.
  • inlet manifold 116 which is preferably configured to receive water from at least four sources, but not all inlets on manifold 1 6 must be used and it may be configured for more than four water sources
  • PAA mixer 120 Mixed water from supply line 1 18 feeds into PAA mixer 120, where it is mixed with PAA from PAA supply tank 122 (which may be a simple chemical drum or barrel).
  • PAA is pumped from PAA supply tank 122, through supply line 124, through control valve assembly 126, through supply line 128 and injection port 130 into mixer 120.
  • Treated water is discharged from mixer 120 through treated water discharge line 138 and into outlet manifold 134.
  • Outlet manifold is preferably configured to discharge to at least five discharge lines, 136a-136e, but not all outlets on outlet manifold must be used and it may be configured for more than five discharge lines.
  • Each discharge line supplies treated water to one or more frac tanks 138a-138e.
  • Water supply lines 114a-1 4d supply water from various sources to inlet ports 160a-160d on intake manifold 1 16. Any standard connections type, such as threaded connectors, may be used to connect water supply lines 14a-1 14d and inlet ports 160a-160d. Preferably, inlet ports 160 are designed to be sealed using known methods when not connected to a supply line 1 14. This allows intake manifold 116 to be used when water is being supplied from fewer water sources 112 than the total number of inlet ports 160. Water from the various sources is then mixed inside intake tube 164 and discharged through mixed water line 118.
  • Flange 166 connects mixed water line 118 to PAA mixer 120, where the water is mixed with PAA and discharged through treated water line 132, connected to PAA mixer by flange 168. Any suitable means of connection may be used to connect water lines 118 and 132 to PAA mixer 120.
  • Mixer 20 or discharge line 132 preferably have a standard sample port (not depicted) for obtaining samples of the treated water shortly after the PAA is injected in order to test the PAA level and make adjustments as described below.
  • a sample port or similar device may be used to allow visual inspection of the mixing quality at or near the treated water output. The PAA quality is measured by residual chemical after demand is met. If it appears that the PAA is not being thoroughly mixed with the intake water, then the PAA injection pressure may be adjusted to increase mixing.
  • PAA is supplied to PAA mixer 120 through injection port 130, which is preferably a threaded aperture in the side of PAA mixer through which an injection quill (discussed below in reference to FIGS. 6-7) is inserted and held in place by quill adapter 185.
  • injection port 130 is preferably a threaded aperture in the side of PAA mixer through which an injection quill (discussed below in reference to FIGS. 6-7) is inserted and held in place by quill adapter 185.
  • mixer 120 is in direct contact with high concentrations PAA, it is preferably constructed of stainless steel.
  • Other parts of the manifold assembly 108 may be made of PVC, carbon steel or other suitable materials.
  • outlet ports 162 are preferably designed to be sealed when not connected to a discharge line 136. This allows outlet manifold 134 to be used when treated water is being supplied to fewer frac tanks 138 than the total number of outlet ports 162.
  • Manifold assembly 108 is preferably mounted on a frame 172, which may then be mounted onto a trailer or flatbed truck, allowing the manifold assembly 108 to be moved to various locations where water treatment for fracturing operations is needed.
  • the control valve assembly 126 discussed below
  • PAA supply tank 122 may also be mounted onto or otherwise secured on the same trailer or flat-bed truck for transport to job-site locations, or these may be separately transported or maintained on-site.
  • Control valve assembly 126 preferably includes ball valve 142, having handle 144, housing 146, and handle 148, and check valve 152, having spring 154 and ball 156.
  • ball 148 is preferably a vented ball, venting upstream when the valve 142 is closed.
  • Check valve 152 is a back- flow prevention valve similar to check valve 52, although in this preferred embodiment an injection quill is used to atomize the PAA, so the check valve 152 does not need to be an atomizer type valve.
  • Ball valve 142 and check valve 152 are standard type valves commonly used in chemical plants and oilfield operations.
  • valves 142 and 152 are connected together and to the PAA supply lines 124 and 128 using known connection methods, such as threaded connections or compression fittings.
  • PAA supply line 128 has a threaded connector 158 that is designed to fit with internal threads 183 on PAA-quill connector 182 (shown on FIGS. 4 and 7), to permit flow of PAA into PAA mixer 120.
  • FIGS. 6, 6B, and 7 depict a preferred embodiment for injection quill 180 for use with apparatus 1 10.
  • Injection quill 180 preferably includes an adapter 185, a quill injection arm 186, nozzle openings 194, and interchangeable nozzles 192.
  • Adapter 185 allows quill arm 186 to be connected to PAA supply line 128 and for quill 180 to be connected to PAA mixer 120.
  • Adapter 185 preferably includes generally cylindrical PAA-quill connector 182, having internal threads 183 and 191 separated by a central bore 187 and having two open ends allowing PAA to freely flow through the adapter from PAA supply line 128 and into quill arm 196. Threaded connector 158 on supply line 128 fits with internal threads 183.
  • Adapter 185 also has external threads 184 on the end having internal threads 191. External threads 184 are designed to fit with the threaded aperture of injection port 130 on PAA mixer 120, allowing quill 180 to be releasably attached to PAA mixer 120. External threads 184 preferably extend from the end of adapter 185 to shoulder 189, which rests against the exterior side of PAA mixer 120 when quill 180 is attached to PAA mixer 120.
  • Quill arm 186 is preferably cylindrical, having an outside diameter of 1 -2 inches, with an open end 181 , a sealed end 188, and a series of nozzle ports 194 connecting to an open central bore extending along the longitudinal axis of quill arm 186.
  • Nozzle ports 194 are preferably threaded apertures in one side of quill arm 186, with the threads being configured to receive threads 196 on nozzle 192.
  • Nozzles 192 are preferably aligned along one side of quill arm 186 in a configuration allowing flow of PAA through the nozzles in a direction that is substantially perpendicular to the longitudinal axis of quill arm 186; however, it may be desirable to have nozzles 192 that direct PAA flow at an another angle relative to quill arm 186 or to have nozzles 192 misaligned relative to each other and any other configuration may be used.
  • Nozzles 192 may be any commercially available nozzles suitable for injection of PAA under high pressure, most preferably around 300 psi or greater. It is preferred that the PAA is atomized upon injection through nozzle opening 198 into mixer 120 so that it is evenly dispersed and can be thoroughly mixed with the intake water inside mixer 120.
  • Different nozzles 192 may have different sized or shaped nozzle openings 198.
  • a different sized nozzle opening 198 may be needed to permit various volumes of PAA discharge depending on the volume of intake water being used. Varying volumes of PAA discharge may also be needed depending on the level of chemical demand of the water sources.
  • Quill 180 is preferably designed to permit interchangeability of various parts to accommodate the particular needs of a fracturing operation and the level of treatment needed for particular water sources.
  • the pressure at which the PAA is introduced into mixer 120 may be varied, such as by adjusting the ball valve 142, as needed to achieve full mixing of the PAA and intake water and to achieve a desired concentration of PAA in the treated water. The methods according to the invention for testing the PAA level and making such adjustments are discussed below.
  • any of several parts such as threads 83, 190, and 191 , quill arm 186, nozzle ports 194/nozzles 192 and nozzle openings 198 can all be modified as needed, provided that adapter 185 and external threads 184 remain sized and configured for connection with injection port 130.
  • Multiple quill arms 186, having different sizes and different nozzles 192 are preferably included as part of apparatus 110, so that they can be quickly changed out as needed on the job site.
  • An injection quill similar to injection quill 180 may also be used with single tank apparatus 10, with suitable modifications that will be understood by those of ordinary skill in the art.
  • FIG. 8 depicts a partial cross-sectional view of a preferred embodiment for insertion of quill 180 into PAA mixer 120.
  • Quill arm 186 is inserted into PAA mixer 120 in an orientation substantially transverse to the direction of water flow from mixed water supply line 1 18.
  • Qui!l arm which is preferably around 12-18 inches long, extends almost all the way across the diameter of PAA mixer 120 along a substantially central axis.
  • Nozzles 192 are preferably aligned facing upstream relative to the direction of water flow. PAA is injected under pressure into mixer 120 through nozzle openings 198 as an atomized, fine mist to fully disperse and mix with the mixed water intake.
  • mixer 120 is sized to provide sufficient residence time of the water and PAA within the mixer to achieve complete mixing; although it is not necessary that there be sufficient residence time to fully treat the water in the mixer, as the PAA will continue treating the water and acting as a biocide while being stored in one or more frac tanks 138.
  • the PAA mixer 120 is fully mixed in with the water. If testing or observation indicate that the PAA is not fully mixed or is not in a desired concentration, according to the methods of the invention discussed below, then adjustments may be made to the volume of PAA or pressure of discharge into mixer 120 to achieve full mixing and desired concentrations.
  • FIGS. 9-1 Another embodiment for a multiple tank apparatus 310 is depicted in FIGS. 9-1 1.
  • Apparatus 310 is shown mounted on a flat-bed trailer 312 allowing it to be easily transported from one job site to another.
  • Apparatus 310 is similar to apparatus 110 except that the outlet ports 362a-h are configured to be elevated relative to the inlet ports 360a-d so that they are substantially at the same height as the top of a typical frac tank.
  • Most frac tanks are designed to accept intake water at an elevated position on the tank (such as that depicted on FIG. 1).
  • apparatus 310 allows the use of a raised platform 316 to access the outlet ports 362, which may be desirable as a safety feature when workers need to make connections from the outlet ports 362 to an elevated access point on the frac tank.
  • Apparatus 310 also includes intake ports 360a-d to receive water from various sources through water supply lines 314a-d, an intake tube 364 for mixing water from the various sources, PAA mixer 120 configured to be connected with control valve assembly 126, outlet tube 370, and manifold frame 372.
  • the configuration and elements of these parts are preferably the same as the corresponding parts for apparatus 110.
  • a method for injecting PAA into water to be used as a frac fluid including the following steps: (1) if intake water from more than one source is being used, mixing intake water from all sources; (2) pumping intake water into a mixer; (3) injecting a sufficient amount of PAA into mixer, preferably using a finely dispersed spray under pressure to achieve thorough mixing with the intake water and to achieve a PAA concentration between 20-60 ppm immediately after mixing; (4) discharging treated water from the mixer to one or more frac tanks.
  • the PAA be injected in the mixer at substantially equidistant locations across the diameter (or other dimension transverse to the direction of intake water flow) of the mixer.
  • the PAA is preferably atomized upon injection into mixer, so the injection is mu!ti-directional; however, it is preferred that the PAA be injected in a direction substantially upstream relative to the direction of intake water flow to aid in mixing of the PAA and intake water. As described above, adequate mixing may be tested by visual inspection and the injection pressure adjusted to increase mixing as necessary.
  • a preferred method for testing the water and adjusting the amount of PAA includes the following steps: (1) collect a representative sample of the water source(s) that will be used in the operation (preferably the water sources used will be at least 70% fresh waters and no more than 30% produced waters); (2) divide the sample into several containers (such as beakers) of a known volume (such as 1 liter or 1 gallon); (3) using a pipette, or other measuring device, dose in a known quantity of PAA into each container; (4) thoroughly mix the samples in each container; (5) following the directions in a commercially available PAA test kit (or using commercially available PAA test strips) measure the concentration in each sample container within approximately 5 minutes of dosing with PAA; (6) if the concentration is below 20 ppm, immediately re-dose with
  • the amount of PAA added to the samples in step 3 is typically between 0.33 gpt (gallons per thousand gallons of water) to 2.94 gpt, depending on the ratio of fresh water sources to produced water sources being used (a higher gpt is needed for higher levels of produced waters).
  • the PAA concentration in the test sample (and in the resulting treated water during operation) will drop over time, which is normal and expected and why testing within a short time of dosing is important.
  • a preferred dosing level is determined based on the quantity of PAA that will give about 20-60 ppm residual PAA immediately after dosing.
  • the amount of PAA needed in operation is then scaled up from the testing dose level to correspond to the volume of intake water that will be treated.
  • a preferred method for such testing includes collecting a representative sample of the treated water, preferably from a sampling port located between mixer 58 and frac tank 38 when using apparatus 10 or preferably between mixer 120 and outlet tube 170 or 370 when using apparatus 110 or 310.
  • the representative sample is tested according to steps (2)-(7) above until the level of PAA is between 20-60 ppm residual, !f necessary, the amount of PAA injected into mixer 58 or 120 is adjusted to an amount corresponding with the dosing amount (adjusted for the amount of intake water being treated relative to the sample size) that was necessary to achieve a PAA concentration of 20-60 ppm.
  • This testing procedure is preferably repeated every 10 minutes, with the results recorded and necessary adjustments made each time.

Abstract

L'invention concerne un procédé et un appareil qui permettent de combiner de multiples sources d'eau d'admission à utiliser dans des opérations de fracturation hydraulique et d'autres opérations de forage pétrolier et gazier et de traiter l'eau avec de l'acide peracétique avant de la déverser dans un ou plusieurs réservoirs de fracturation ou dans un puits. L'appareil comprend un ensemble collecteur qui combine de l'eau issue de sources multiples avant de la faire entrer dans un mélangeur dans lequel est injecté de l'acide peracétique (APA) sous forme de dispersion fine pulvérisée sous pression pour mélanger intimement l'APA et l'eau d'admission avant que le mélange soit déversé dans un ou plusieurs réservoirs de fracturation. L'utilisation d'un ensemble collecteur permet de transporter facilement l'appareil à différents endroits/sites de travail et d'utiliser des raccords standard pour assurer un raccordement aisé entre l'appareil et un équipement de fracturation existant. L'invention concerne également un procédé d'injection d'APA et d'essai et d'ajustement du niveau d'APA.
PCT/US2012/063902 2011-11-07 2012-11-07 Système et procédé d'injection d'acide peracétique WO2013070728A1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US201161556490P 2011-11-07 2011-11-07
US61/556,490 2011-11-07

Publications (1)

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WO2013070728A1 true WO2013070728A1 (fr) 2013-05-16

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2015081328A1 (fr) * 2013-11-28 2015-06-04 Data Automated Water Systems, LLC Système automatisé de surveillance et de commande de transfert d'eau durant une fracturation hydraulique

Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4676563A (en) * 1985-05-06 1987-06-30 Innotech Energy Corporation Apparatus for coupling multi-conduit drill pipes
EP0482930A2 (fr) * 1990-10-24 1992-04-29 Baker Hughes Incorporated Dispositif de mélange
US20040200619A1 (en) * 2002-09-24 2004-10-14 Bj Services Company Compositions containing a buffer and a peroxide or peracid useful for treating wells
US20050269080A1 (en) * 2004-06-03 2005-12-08 Cowan Kenneth M Method and apparatus for performing chemical treatments of exposed geological formations
US20080095677A1 (en) * 2006-10-18 2008-04-24 Mcsherry David D Apparatus and method for making a peroxycarboxylic acid
US20090147616A1 (en) * 2006-01-30 2009-06-11 Kimmo Leinonen Method of and Apparatus For Controlling The Efficiency of Mixing
US20090311134A1 (en) * 2006-06-21 2009-12-17 Toyo Seikan Kaisha, Ltd. Sterilants and sterilization method for aseptic filling
US20100160449A1 (en) * 2008-12-18 2010-06-24 Fmc Corporation Peracetic Acid Oil-Field Biocide and Method
US8245784B2 (en) * 2010-06-07 2012-08-21 Halliburton Energy Services, Inc. Stable organic-based fluid loss additive containing an organophilic clay-based suspending agent for use in a well

Patent Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4676563A (en) * 1985-05-06 1987-06-30 Innotech Energy Corporation Apparatus for coupling multi-conduit drill pipes
EP0482930A2 (fr) * 1990-10-24 1992-04-29 Baker Hughes Incorporated Dispositif de mélange
US20040200619A1 (en) * 2002-09-24 2004-10-14 Bj Services Company Compositions containing a buffer and a peroxide or peracid useful for treating wells
US20050269080A1 (en) * 2004-06-03 2005-12-08 Cowan Kenneth M Method and apparatus for performing chemical treatments of exposed geological formations
US20090147616A1 (en) * 2006-01-30 2009-06-11 Kimmo Leinonen Method of and Apparatus For Controlling The Efficiency of Mixing
US20090311134A1 (en) * 2006-06-21 2009-12-17 Toyo Seikan Kaisha, Ltd. Sterilants and sterilization method for aseptic filling
US20080095677A1 (en) * 2006-10-18 2008-04-24 Mcsherry David D Apparatus and method for making a peroxycarboxylic acid
US20100160449A1 (en) * 2008-12-18 2010-06-24 Fmc Corporation Peracetic Acid Oil-Field Biocide and Method
US8245784B2 (en) * 2010-06-07 2012-08-21 Halliburton Energy Services, Inc. Stable organic-based fluid loss additive containing an organophilic clay-based suspending agent for use in a well

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2015081328A1 (fr) * 2013-11-28 2015-06-04 Data Automated Water Systems, LLC Système automatisé de surveillance et de commande de transfert d'eau durant une fracturation hydraulique
US10711584B2 (en) 2013-11-28 2020-07-14 Select Energy Services, Llc Automated system for monitoring and controlling water transfer during hydraulic fracturing
US11578578B2 (en) 2013-11-28 2023-02-14 Select Energy Services, Llc Automated system for monitoring and controlling water transfer during hydraulic fracturing

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