US20180311634A1 - Systems and methods of treating water used for hydraulic fracturing - Google Patents
Systems and methods of treating water used for hydraulic fracturing Download PDFInfo
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- US20180311634A1 US20180311634A1 US16/029,915 US201816029915A US2018311634A1 US 20180311634 A1 US20180311634 A1 US 20180311634A1 US 201816029915 A US201816029915 A US 201816029915A US 2018311634 A1 US2018311634 A1 US 2018311634A1
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/0006—Controlling or regulating processes
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/68—Treatment of water, waste water, or sewage by addition of specified substances, e.g. trace elements, for ameliorating potable water
- C02F1/685—Devices for dosing the additives
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/72—Treatment of water, waste water, or sewage by oxidation
- C02F1/76—Treatment of water, waste water, or sewage by oxidation with halogens or compounds of halogens
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/72—Treatment of water, waste water, or sewage by oxidation
- C02F1/76—Treatment of water, waste water, or sewage by oxidation with halogens or compounds of halogens
- C02F1/763—Devices for the addition of such compounds in gaseous form
-
- 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
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00051—Controlling the temperature
- B01J2219/00054—Controlling or regulating the heat exchange system
- B01J2219/00056—Controlling or regulating the heat exchange system involving measured parameters
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00051—Controlling the temperature
- B01J2219/00054—Controlling or regulating the heat exchange system
- B01J2219/00056—Controlling or regulating the heat exchange system involving measured parameters
- B01J2219/00069—Flow rate measurement
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/10—Nature of the water, waste water, sewage or sludge to be treated from quarries or from mining activities
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/04—Disinfection
Definitions
- Hydraulic fracturing refers to a process in which a wellbore is drilled into a rock formation, and a fracturing fluid is then pumped into the wellbore under great pressure to induce an initial set of fractures in the rock formation. The fracturing fluid is then forced into the initial fractures, extending the fractures further. An operator may then introduce a proppant into the fracturing fluid that is being pumped into the fractures, such as sand, ceramic particles to other particulates. The proppant is designed to prevent the fractures from closing when the fracturing fluid pressure is reduced or when pumping stops.
- the fracturing fluid which is pumped into the wellbore typically includes water.
- various chemicals and materials are added to the water for various purposes.
- the chemicals that are added can depend upon the type of well and the underground rock formations that are being fractured.
- friction reducing additives can be used to increase the flow rate and to reduce the pressure needed to pump the fracturing fluid into the well.
- Oxygen scavengers and other stabilizers and corrosion inhibitors can be added to prevent corrosion of the pipes.
- Acid such as hydrochloric acid, can be added to help dissolve minerals and induce fractures.
- Surfactants and crosslinking agents help to maintain fluid viscosity, particularly as temperature increases.
- Gels can be added to help suspend greater amounts of proppants in the fracturing fluid.
- a scale inhibitor may be added to prevent scale deposits in the pipes.
- a pH adjusting agent may be added to maintain the effectiveness of the other agents, particularly the crosslinkers.
- various biocides may be added to eliminate bacteria which can produce corrosive byproducts that attack the pipes.
- the biocides that are added to fracturing fluid can include glutaraldehyde, quaternary amines, active liquid brominated propionamide solutions and other materials. It is important that any biocide added to the fracturing fluid not disrupt or inhibit the functions performed by the other additives.
- FIG. 1 is flow diagram illustrating a method of treating a fracturing fluid with a biocide
- FIG. 2 is a diagram of a system for treating a fracturing fluid with a biocide
- FIG. 3 is a diagram of an alternate system for treating a fracturing fluid with a biocide.
- chlorine dioxide can be used as an effective biocide in fracturing fluids.
- Chlorine dioxide in appropriate concentrations can be as effective, or more effective, in eliminating harmful bacteria in fracturing fluid than known biocides used for this purpose, such as glutaraldehyde, quaternary amines, and active liquid brominated propionamide solutions.
- biocides used for this purpose such as glutaraldehyde, quaternary amines, and active liquid brominated propionamide solutions.
- chlorine dioxide is an EPA approved material for use as a biocide because it is not harmful to humans, animals or the environment when used in the low dosages and concentrations required for effective use as a biocide.
- Chlorine dioxide can be formed in many different ways. Some of the reactions which produce chlorine dioxide result in the formation of free chlorine, which is undesirable. However, the inventor has determined that an effective reaction that produces chlorine dioxide that can be used as a biocide in fracturing fluid, and which does not result in the production of free chlorine is the reaction formula:
- FIG. 1 A flowchart illustrating a method embodying the invention for treating a fluid that is to be used for hydraulic fracturing is presented in FIG. 1 .
- the method begins in step S 102 , where a supply of chlorine dioxide is either obtained or generated. If the chlorine dioxide is to be generated, it is preferably generated according to the reaction formula illustrated above. In alternate embodiments, a supply of chlorine dioxide could be generated in other ways. In still other alternate embodiments, a supply of chlorine dioxide could simply be obtained from a source.
- step S 104 the obtained or generated chlorine dioxide is added to a flow of fluid which is to be used for hydraulic fracturing.
- the chlorine dioxide is added in an amount that results in the concentration of the chlorine dioxide in the fracturing fluid being high enough to act as an effective biocide to kill harmful bacteria that may be present in the fracturing fluid.
- the concentration should also be low enough that the residual chlorine dioxide present in the fracturing fluid will not be harmful to humans, animals or the environment.
- the concentration must also remain low enough to prevent the chlorine dioxide from interfering with the functions performed by the other additives and chemicals that are present in the fracturing fluid. Desirable residual concentrations are generally within the range of 0.1 to 0.8 parts per million.
- the inventor has developed a treatment system which continuously mixes chlorine dioxide into an incoming flow of fluid which is to be used for hydraulic fracturing.
- the treatment system developed by the inventor can perform a method as illustrated in FIG. 1 .
- the flow can be immediately used for hydraulic fracturing, or the treated fluid can be collected in a storage tank before the treated fluid is actually pumped into a wellbore during a hydraulic fracturing process.
- FIG. 2 A first embodiment of such a treatment system is illustrated in FIG. 2 .
- a fluid supply pipe 110 receives a flow of fluid that is to be used for hydraulic fracturing.
- the fluid flows along the supply pipe 110 to an outlet end 118 which delivers the fluid to a fracturing fluid storage tank 130 .
- chlorine dioxide is added to the fluid by a chlorine dioxide treating unit 120 .
- a header 112 installed in the fluid pipe 110 includes an inlet pipe 113 that is attached to an inlet 121 of the chlorine dioxide treating unit 120 .
- An outlet pipe 115 which is attached to an outlet 123 of the chlorine dioxide treating unit delivers treated fluid back into the supply pipe 110 via the header 112 .
- a relatively small percentage of the fluid flowing through the supply pipe 110 is routed through the header 112 , the inlet pipe 113 and the inlet 121 into the chlorine dioxide treating unit 120 .
- Chlorine dioxide is added to the received fluid, and the treated fluid is send back into the supply pipe 110 via the outlet 123 , outlet pipe 115 and the header 112 .
- the treated fluid mixes with the fluid in the supply pipe 110 as it travels along the supply pipe 110 to the outlet 118 and into the fracturing fluid storage tank 130 .
- the fluid in the supply pipe 110 is typically under pressure.
- the flow of fluid through the inlet pipe 113 , the chlorine dioxide treating unit 120 and the outlet pipe 115 will generate flow losses which result in the fluid in the outlet pipe being at a lower pressure than the fluid in the supply pipe 110 .
- a booster pump 125 located on the inlet pipe 113 can be used for this purpose.
- the booster pump 125 could be located at alternate positions, such as within the chlorine dioxide treating unit 120 , or on the outlet pipe 115 .
- the chlorine dioxide treating unit 120 may receive a supply of chlorine dioxide that is added to the fluid.
- the chlorine dioxide treating unit 120 may include a first supply reservoir 122 , a second supply reservoir 124 , and a third supply reservoir 126 .
- the first supply reservoir 122 contains a supply of sodium chlorite
- the second supply reservoir 124 contains a supply of hydrochloric acid.
- the third supply reservoir 126 contains a supply of fresh water.
- the chlorine dioxide treating unit 120 utilizes the sodium chlorite, hydrochloric acid and fresh water to generate chlorine dioxide which is then added to the fluid.
- the chlorine dioxide treating unit 120 may include a flow meter.
- a flow meter could be installed on the header 112 , the inlet pipe 113 , or the outlet pipe 115 .
- the flow meter would indicate the flow rate of the fluid passing through the chlorine dioxide treating unit 120 , and this information could be used to determine the appropriate amount of chlorine dioxide to add to the fluid.
- a test header 116 having a sample pipe 117 is connected to the fluid supply pipe 110 downstream from the header 112 .
- the sample pipe 117 conveys a sample of the treated fluid back to the chlorine dioxide treating unit 120 , which checks the concentration of chlorine dioxide in the fluid collected through the sample pipe 117 .
- the chlorine dioxide treating unit can then selectively vary the amount of chlorine dioxide being added to the fluid to achieve the proper concentration of chlorine dioxide in the fluid.
- control valves 142 and 144 are installed on the inlet pipe 113 and outlet pipe 115 , respectively.
- a controller 140 is coupled to the control valves 142 , 144 and to the chlorine dioxide treating unit 120 .
- the controller 140 selectively varies the flow rate of the fluid through the chlorine dioxide treating unit 120 to control the amount of chlorine dioxide that is added to the fracturing fluid in the supply pipe 110 .
- the controller 140 may also, or alternatively, exert control over the amount of chlorine dioxide that the chlorine dioxide treating unit 120 is adding to the fluid.
- the controller 140 could be used ensure that the appropriate amount of chlorine dioxide is being added to the fluid.
- a control valve 146 may also be installed in the sample line 117 that is connected to the test header 116 .
- the controller 140 may also be coupled to the control valve 146 to control the flow of fluid through the sample line 117 .
- the fluid being delivered into the supply pipe 110 can be acquired from many different sources in different fracturing operations. Often the fluid is acquired from a local lake or pond, from a well, or the fluid is delivered via a tanker truck. In some instances, it may be possible to acquire water from a local water supply system operated by a municipality or a city. Because the fluid can be acquired from many different sources, there can be different amounts of bacteria or other biological contaminants which are to be partially or fully eliminated by the chlorine dioxide treatment.
- the chlorine dioxide that is added to the fluid is basically consumed in chemical reactions in order to eliminate the bacteria or other biological contaminants that are present in the fluid. Thus, some or all of the chlorine dioxide added to the fluid in the supply pipe 110 via the chlorine dioxide treating unit 120 will be consumed before the fluid is ultimately used in a fracturing operation.
- the residual amount of chlorine dioxide that is present in the fluid ultimately used in a fracturing operation is in the range of 0.1 to 0.8 ppm.
- the chlorine dioxide treating unit 120 can be adjusted to insert greater amounts of chlorine dioxide into the fluid, or vice versa. Periodic testing may be required to continually adjust the amount of chlorine dioxide that is being added to the fluid in the fluid supply pipe 110 to ensure that the residual chlorine dioxide concentration in the fluid being used in fracturing operations is within the desirable range.
- the sample pipe 117 may be located sufficiently far downstream that the bacteria and other biological contaminants originally present in the supply water will have been largely eliminated by the chlorine dioxide before a sample of the fluid is drawn through the sample pipe 117 .
- measuring the concentration of the chlorine dioxide in the fluid drawn from the sample pipe 117 may provide the information needed to continually adjust the amount of chlorine dioxide being added by the chlorine dioxide treating unit 120 to achieve a desirable residual chlorine dioxide concentration. This may make it possible for the controller 140 to provide automated control of the amount of chlorine dioxide that is added.
- manual samples of the fluid may be drawn from other locations that are farther downstream, such as from a location just before the fluid is used in a fracturing operation. In that instance, it may be necessary for an operator to manually adjust the amount of chlorine dioxide that is being added by the chlorine dioxide treating unit 120 .
- FIG. 3 illustrates an alternate embodiment of the system which is similar to the one discussed above in connection with FIG. 2 . Accordingly, only the differences will be discussed.
- the booster pump 125 is located on the outlet line 115 connected to the chlorine dioxide treating unit 120 , instead of the inlet line 113 .
- first and second headers 112 , 114 are used to draw fluid from the supply pipe 110 , and return treated fluid to the supply pipe 110 , respectively.
- the sample pipe 117 connected to the test header 116 is coupled to an analyzer unit 150 .
- the analyzer unit 150 determines a concentration of chlorine dioxide in the fluid obtained through the sample pipe 117 .
- the analyzer unit 150 then sends a signal to the chlorine dioxide treating unit 120 via a control line 154 , the signal being representative of the determined chlorine dioxide concentration.
- the chlorine dioxide treating unit 120 uses the signal to selectively adjust the amount of chlorine dioxide being added to the fluid to achieve a desired residual chlorine dioxide concentration in the fracturing fluid.
- the analyzer unit 150 may be coupled to a controller 140 via a signal line 152 , so that a signal representative of the determined chlorine dioxide concentration is received by the controller 140 .
- the controller 140 may then instruct the chlorine dioxide treating unit 120 to selectively adjust the amount of chlorine dioxide being added to the fluid.
- the controller 140 could utilize the signal from the analyzer unit 150 to selectively vary a flow rate through the chlorine dioxide treating unit 120 , via one or both of the control valves 142 , 144 to adjust the amount of chlorine dioxide being added to the fluid.
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Abstract
A system and method of treating a fluid to be used for hydraulic fracturing adds an effective amount of chlorine dioxide to the fluid to act as a biocide that kills harmful bacteria. A system for adding chlorine dioxide to the fluid can continuously add chlorine dioxide to an incoming flow of the fluid to produce a continuous flow of treated fluid.
Description
- This application is a divisional application of U.S. application Ser. No. 15/150,228, filed May 9, 2016, is a continuation of U.S. application Ser. No. 14/106,052, filed Dec. 13, 2013, now issued as U.S. Pat. No. 9,358,517, which is a continuation of U.S. application Ser. No. 14/020,495, filed Sep. 6, 2013, now issued as U.S. Pat. No. 8,962,534, which itself claims priority to U.S. Provisional Application No. 61/697,932, filed Sep. 7, 2012, the entire contents of which are hereby incorporated by reference.
- Hydraulic fracturing refers to a process in which a wellbore is drilled into a rock formation, and a fracturing fluid is then pumped into the wellbore under great pressure to induce an initial set of fractures in the rock formation. The fracturing fluid is then forced into the initial fractures, extending the fractures further. An operator may then introduce a proppant into the fracturing fluid that is being pumped into the fractures, such as sand, ceramic particles to other particulates. The proppant is designed to prevent the fractures from closing when the fracturing fluid pressure is reduced or when pumping stops.
- Once the fracturing process is complete, petroleum, natural gas and other fluids which are under considerable pressure in the rock formation escape through the fractures and into the wellbore. The petroleum and natural gas is ultimately extracted through the fractures and the wellbore and is captured and stored. During the initial stages after the fracturing is completed, the petroleum and natural gas may push much of the fracturing fluid back up the well bore. However, it is also common for a significant percentage of the fracturing fluid to disperse into the surrounding rock through the fractures that were created.
- The fracturing fluid which is pumped into the wellbore typically includes water. However, various chemicals and materials are added to the water for various purposes. The chemicals that are added can depend upon the type of well and the underground rock formations that are being fractured. In addition to the proppants mentioned above, friction reducing additives can be used to increase the flow rate and to reduce the pressure needed to pump the fracturing fluid into the well. Oxygen scavengers and other stabilizers and corrosion inhibitors can be added to prevent corrosion of the pipes. Acid, such as hydrochloric acid, can be added to help dissolve minerals and induce fractures. Surfactants and crosslinking agents help to maintain fluid viscosity, particularly as temperature increases. Gels can be added to help suspend greater amounts of proppants in the fracturing fluid. A scale inhibitor may be added to prevent scale deposits in the pipes. A pH adjusting agent may be added to maintain the effectiveness of the other agents, particularly the crosslinkers. Finally, various biocides may be added to eliminate bacteria which can produce corrosive byproducts that attack the pipes. The biocides that are added to fracturing fluid can include glutaraldehyde, quaternary amines, active liquid brominated propionamide solutions and other materials. It is important that any biocide added to the fracturing fluid not disrupt or inhibit the functions performed by the other additives.
- Because the fracturing fluid can escape into the surrounding rock formations, and ultimately propagate into the water table, there is great concern about the chemical additives that are present in the fracturing fluid. Thus, operators are seeking to use chemicals which are known to be safe to humans, animals and the environment.
-
FIG. 1 is flow diagram illustrating a method of treating a fracturing fluid with a biocide; -
FIG. 2 is a diagram of a system for treating a fracturing fluid with a biocide; and -
FIG. 3 is a diagram of an alternate system for treating a fracturing fluid with a biocide. - The inventor has discovered that chlorine dioxide can be used as an effective biocide in fracturing fluids. Chlorine dioxide in appropriate concentrations can be as effective, or more effective, in eliminating harmful bacteria in fracturing fluid than known biocides used for this purpose, such as glutaraldehyde, quaternary amines, and active liquid brominated propionamide solutions. In addition, chlorine dioxide is an EPA approved material for use as a biocide because it is not harmful to humans, animals or the environment when used in the low dosages and concentrations required for effective use as a biocide.
- Chlorine dioxide can be formed in many different ways. Some of the reactions which produce chlorine dioxide result in the formation of free chlorine, which is undesirable. However, the inventor has determined that an effective reaction that produces chlorine dioxide that can be used as a biocide in fracturing fluid, and which does not result in the production of free chlorine is the reaction formula:
-
5 NaClO2+4 HCl→5NaCl+4ClO2+2H2O. - A flowchart illustrating a method embodying the invention for treating a fluid that is to be used for hydraulic fracturing is presented in
FIG. 1 . As shown inFIG. 1 , the method begins in step S102, where a supply of chlorine dioxide is either obtained or generated. If the chlorine dioxide is to be generated, it is preferably generated according to the reaction formula illustrated above. In alternate embodiments, a supply of chlorine dioxide could be generated in other ways. In still other alternate embodiments, a supply of chlorine dioxide could simply be obtained from a source. - In step S104, the obtained or generated chlorine dioxide is added to a flow of fluid which is to be used for hydraulic fracturing. The chlorine dioxide is added in an amount that results in the concentration of the chlorine dioxide in the fracturing fluid being high enough to act as an effective biocide to kill harmful bacteria that may be present in the fracturing fluid. However, the concentration should also be low enough that the residual chlorine dioxide present in the fracturing fluid will not be harmful to humans, animals or the environment. The concentration must also remain low enough to prevent the chlorine dioxide from interfering with the functions performed by the other additives and chemicals that are present in the fracturing fluid. Desirable residual concentrations are generally within the range of 0.1 to 0.8 parts per million.
- The inventor has developed a treatment system which continuously mixes chlorine dioxide into an incoming flow of fluid which is to be used for hydraulic fracturing. Thus, the treatment system developed by the inventor can perform a method as illustrated in
FIG. 1 . Once the treatment system has added chlorine dioxide to the incoming flow, the flow can be immediately used for hydraulic fracturing, or the treated fluid can be collected in a storage tank before the treated fluid is actually pumped into a wellbore during a hydraulic fracturing process. - A first embodiment of such a treatment system is illustrated in
FIG. 2 . As shown therein, afluid supply pipe 110 receives a flow of fluid that is to be used for hydraulic fracturing. The fluid flows along thesupply pipe 110 to anoutlet end 118 which delivers the fluid to a fracturingfluid storage tank 130. As the fluid flows along thesupply pipe 110, chlorine dioxide is added to the fluid by a chlorinedioxide treating unit 120. - As shown in
FIG. 2 , aheader 112 installed in thefluid pipe 110 includes aninlet pipe 113 that is attached to aninlet 121 of the chlorinedioxide treating unit 120. Anoutlet pipe 115 which is attached to anoutlet 123 of the chlorine dioxide treating unit delivers treated fluid back into thesupply pipe 110 via theheader 112. - In operation, a relatively small percentage of the fluid flowing through the
supply pipe 110 is routed through theheader 112, theinlet pipe 113 and theinlet 121 into the chlorinedioxide treating unit 120. Chlorine dioxide is added to the received fluid, and the treated fluid is send back into thesupply pipe 110 via theoutlet 123,outlet pipe 115 and theheader 112. The treated fluid mixes with the fluid in thesupply pipe 110 as it travels along thesupply pipe 110 to theoutlet 118 and into the fracturingfluid storage tank 130. - The fluid in the
supply pipe 110 is typically under pressure. The flow of fluid through theinlet pipe 113, the chlorinedioxide treating unit 120 and theoutlet pipe 115 will generate flow losses which result in the fluid in the outlet pipe being at a lower pressure than the fluid in thesupply pipe 110. In order to force the treated fluid from theoutlet pipe 115 back into thefluid supply pipe 110, it is necessary to raise the pressure of the fluid in theoutlet pipe 115. Abooster pump 125 located on theinlet pipe 113 can be used for this purpose. However, thebooster pump 125 could be located at alternate positions, such as within the chlorinedioxide treating unit 120, or on theoutlet pipe 115. - In some embodiments, the chlorine
dioxide treating unit 120 may receive a supply of chlorine dioxide that is added to the fluid. In alternate embodiments, the chlorinedioxide treating unit 120 may include afirst supply reservoir 122, asecond supply reservoir 124, and athird supply reservoir 126. Thefirst supply reservoir 122 contains a supply of sodium chlorite, and thesecond supply reservoir 124 contains a supply of hydrochloric acid. Thethird supply reservoir 126 contains a supply of fresh water. The chlorinedioxide treating unit 120 utilizes the sodium chlorite, hydrochloric acid and fresh water to generate chlorine dioxide which is then added to the fluid. - In some embodiments, the chlorine
dioxide treating unit 120 may include a flow meter. Alternatively, a flow meter could be installed on theheader 112, theinlet pipe 113, or theoutlet pipe 115. In such an embodiment, the flow meter would indicate the flow rate of the fluid passing through the chlorinedioxide treating unit 120, and this information could be used to determine the appropriate amount of chlorine dioxide to add to the fluid. - In alternate embodiments, a
test header 116 having asample pipe 117 is connected to thefluid supply pipe 110 downstream from theheader 112. Thesample pipe 117 conveys a sample of the treated fluid back to the chlorinedioxide treating unit 120, which checks the concentration of chlorine dioxide in the fluid collected through thesample pipe 117. The chlorine dioxide treating unit can then selectively vary the amount of chlorine dioxide being added to the fluid to achieve the proper concentration of chlorine dioxide in the fluid. By sampling the fluid from a location well downstream of where the treated fluid is delivered back into thesupply pipe 110, it is possible to ensure that the treated fluid delivered into thesupply pipe 110 via theoutlet pipe 115 has fully mixed with the fluid in thesupply pipe 110 such that a final resulting chlorine dioxide concentration has been achieved. - As also illustrated in
FIG. 2 , in some embodiments controlvalves inlet pipe 113 andoutlet pipe 115, respectively. Acontroller 140 is coupled to thecontrol valves dioxide treating unit 120. In this embodiment, thecontroller 140 selectively varies the flow rate of the fluid through the chlorinedioxide treating unit 120 to control the amount of chlorine dioxide that is added to the fracturing fluid in thesupply pipe 110. Thecontroller 140 may also, or alternatively, exert control over the amount of chlorine dioxide that the chlorinedioxide treating unit 120 is adding to the fluid. Thus, thecontroller 140 could be used ensure that the appropriate amount of chlorine dioxide is being added to the fluid. - In some instances, a
control valve 146 may also be installed in thesample line 117 that is connected to thetest header 116. In those embodiments, thecontroller 140 may also be coupled to thecontrol valve 146 to control the flow of fluid through thesample line 117. - The fluid being delivered into the
supply pipe 110 can be acquired from many different sources in different fracturing operations. Often the fluid is acquired from a local lake or pond, from a well, or the fluid is delivered via a tanker truck. In some instances, it may be possible to acquire water from a local water supply system operated by a municipality or a city. Because the fluid can be acquired from many different sources, there can be different amounts of bacteria or other biological contaminants which are to be partially or fully eliminated by the chlorine dioxide treatment. - The chlorine dioxide that is added to the fluid is basically consumed in chemical reactions in order to eliminate the bacteria or other biological contaminants that are present in the fluid. Thus, some or all of the chlorine dioxide added to the fluid in the
supply pipe 110 via the chlorinedioxide treating unit 120 will be consumed before the fluid is ultimately used in a fracturing operation. - It is desirable for the residual amount of chlorine dioxide that is present in the fluid ultimately used in a fracturing operation to be in the range of 0.1 to 0.8 ppm. However, one cannot simply add an amount of chlorine dioxide to the fluid in the
supply pipe 110 in a predetermined volume amount to achieve this concentration because some of the chlorine dioxide that is added to the fluid will be consumed in eliminating bacteria and other biological contaminants that were present in the fluid being supplied into thefluid supply pipe 110. And because one can never be certain how much bacteria or other biological contaminants are present in the supply water, one can never know in advance how much chlorine dioxide will be consumed. - Because of these factors, it is desirable to test the fluid in the fluid
fracturing storage tank 130, or perhaps even farther downstream in the supply chain to determine the actual residual chlorine dioxide concentration in the fracturing fluid once some of the chlorine dioxide has been consumed in eliminating bacteria and other biological contaminants. If the residual chlorine dioxide concentration is too low, the chlorinedioxide treating unit 120 can be adjusted to insert greater amounts of chlorine dioxide into the fluid, or vice versa. Periodic testing may be required to continually adjust the amount of chlorine dioxide that is being added to the fluid in thefluid supply pipe 110 to ensure that the residual chlorine dioxide concentration in the fluid being used in fracturing operations is within the desirable range. - In some embodiments, the
sample pipe 117 may be located sufficiently far downstream that the bacteria and other biological contaminants originally present in the supply water will have been largely eliminated by the chlorine dioxide before a sample of the fluid is drawn through thesample pipe 117. Thus, measuring the concentration of the chlorine dioxide in the fluid drawn from thesample pipe 117 may provide the information needed to continually adjust the amount of chlorine dioxide being added by the chlorinedioxide treating unit 120 to achieve a desirable residual chlorine dioxide concentration. This may make it possible for thecontroller 140 to provide automated control of the amount of chlorine dioxide that is added. - In other embodiments, manual samples of the fluid may be drawn from other locations that are farther downstream, such as from a location just before the fluid is used in a fracturing operation. In that instance, it may be necessary for an operator to manually adjust the amount of chlorine dioxide that is being added by the chlorine
dioxide treating unit 120. -
FIG. 3 illustrates an alternate embodiment of the system which is similar to the one discussed above in connection withFIG. 2 . Accordingly, only the differences will be discussed. - In the embodiment illustrated in
FIG. 3 , thebooster pump 125 is located on theoutlet line 115 connected to the chlorinedioxide treating unit 120, instead of theinlet line 113. Also, instead of asingle header 112, first andsecond headers supply pipe 110, and return treated fluid to thesupply pipe 110, respectively. Also, thesample pipe 117 connected to thetest header 116 is coupled to ananalyzer unit 150. Theanalyzer unit 150 determines a concentration of chlorine dioxide in the fluid obtained through thesample pipe 117. Theanalyzer unit 150 then sends a signal to the chlorinedioxide treating unit 120 via acontrol line 154, the signal being representative of the determined chlorine dioxide concentration. The chlorinedioxide treating unit 120 uses the signal to selectively adjust the amount of chlorine dioxide being added to the fluid to achieve a desired residual chlorine dioxide concentration in the fracturing fluid. - In an alternate embodiment, the
analyzer unit 150 may be coupled to acontroller 140 via asignal line 152, so that a signal representative of the determined chlorine dioxide concentration is received by thecontroller 140. Thecontroller 140 may then instruct the chlorinedioxide treating unit 120 to selectively adjust the amount of chlorine dioxide being added to the fluid. Alternatively, or in addition, thecontroller 140 could utilize the signal from theanalyzer unit 150 to selectively vary a flow rate through the chlorinedioxide treating unit 120, via one or both of thecontrol valves - The terminology used herein is for the purpose of describing particular embodiments only and is not intended to be limiting of the invention. As used herein, the singular forms “a”, “an” and “the” are intended to include the plural forms as well, unless the context clearly indicates otherwise. It will be further understood that the terms “comprises” and/or “comprising,” when used in this specification, specify the presence of stated features, integers, steps, operations, elements, and/or components, but do not preclude the presence or addition of one or more other features, integers, steps, operations, elements, components, and/or groups thereof.
- While the invention has been described in connection with what is presently considered to be the most practical and preferred embodiment, it is to be understood that the invention is not to be limited to the disclosed embodiment, but on the contrary, is intended to cover various modifications and equivalent arrangements included within the spirit and scope of the appended claims.
Claims (10)
1. A method of treating a fluid used for hydraulic fracturing, comprising:
obtaining chlorine dioxide;
adding an amount of the obtained chlorine dioxide to a continuously supplied fluid which is to be used for hydraulic fracturing such that the chlorine dioxide acts as a biocide, wherein a prescribed amount of the chlorine dioxide is added per unit volume of the continuously supplied fluid;
periodically testing the continuously supplied fluid after the chlorine dioxide has been added and after at least some of the chlorine dioxide has been consumed in reactions with bacteria and/or biological contaminants that were originally present in the fluid to determine a concentration of the chlorine dioxide in the supplied fluid; and
selectively adjusting the prescribed amount of chlorine dioxide that is added per unit volume of the continuously supplied fluid based on the result of the testing step such that a residual concentration of chlorine dioxide remaining in the fluid after the chlorine dioxide has had an opportunity to react with bacteria and/or biological contaminants is in the range of 0.1 to 25 parts per million.
2. The method of claim 1 , wherein the adjusting step is performed such that a residual concentration of chlorine dioxide remaining in the fluid after the chlorine dioxide has had an opportunity to react with bacteria and/or biological contaminants is in the range of 0.1 to 0.8 parts per million.
3. The method of claim 1 , wherein the step of obtaining chlorine dioxide comprises reacting sodium chlorite with hydrochloric acid to produce chlorine dioxide.
4. The method of claim 1 , wherein the reaction that produces the chlorine dioxide proceeds according to the following chemical equation:
5 NaClO2+4 HCl→5NaCl+4ClO2+2H2O.
5 NaClO2+4 HCl→5NaCl+4ClO2+2H2O.
5. The method of claim 1 , wherein the adding step comprises:
diverting a portion of the continuously supplied fluid from a main supply pipe to a treatment unit;
adding the prescribed amount of the obtained chlorine dioxide to a unit volume of the diverted fluid to create a flow of treated fluid; and
delivering the flow of treated fluid back into the main supply pipe.
6. The method of claim 5 , wherein the periodic testing is performed on fluid drawn from the main supply pipe at a location that is downstream from where the treated fluid is delivered back into the main supply pipe.
7. A method of treating a fluid used for hydraulic fracturing, comprising:
obtaining chlorine dioxide;
diverting a predetermined flow rate of a continuously supplied fluid that is to be used for hydraulic fracturing from a main supply pipe to a treatment unit;
adding a substantially constant flow rate of the obtained chlorine dioxide to the diverted flow of fluid to create a flow of treated fluid;
delivering the flow of treated fluid back into the main supply pipe;
periodically testing fluid drawn from the main supply pipe at a location that is downstream from where the treated fluid is delivered back into the main supply pipe, and after at least some of the chlorine dioxide has been consumed in reactions with bacteria and/or biological contaminants that were originally present in the fluid, to determine a concentration of the chlorine dioxide in the tested fluid; and
selectively adjusting the flow rate of the fluid that is diverted from the main supply pipe into the treatment unit based on the result of the testing step such that a residual concentration of chlorine dioxide remaining in the fluid after the chlorine dioxide has had an opportunity to react with bacteria and/or biological contaminants is in the range of 0.1 to 25 parts per million.
8. The method of claim 7 , wherein the adjusting step is performed such that a residual concentration of chlorine dioxide remaining in the fluid after the chlorine dioxide has had an opportunity to react with bacteria and/or biological contaminants is in the range of 0.1 to 0.8 parts per million.
9. The method of claim 7 , wherein the step of obtaining chlorine dioxide comprises reacting sodium chlorite with hydrochloric acid to produce chlorine dioxide.
10. The method of claim 9 , wherein the reaction that produces the chlorine dioxide proceeds according to the following chemical equation:
5 NaClO2+4 HCl→5NaCl+4ClO2+2H2O.
5 NaClO2+4 HCl→5NaCl+4ClO2+2H2O.
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US16/029,915 US20180311634A1 (en) | 2012-09-07 | 2018-07-09 | Systems and methods of treating water used for hydraulic fracturing |
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US201261697932P | 2012-09-07 | 2012-09-07 | |
US14/020,495 US8962534B2 (en) | 2012-09-07 | 2013-09-06 | Systems and methods of treating water used for hydraulic fracturing |
US14/106,052 US9358517B2 (en) | 2012-09-07 | 2013-12-13 | Systems and methods of treating water used for hydraulic fracturing |
US15/150,228 US10040046B2 (en) | 2012-09-07 | 2016-05-09 | Systems and methods of treating water used for hydraulic fracturing |
US16/029,915 US20180311634A1 (en) | 2012-09-07 | 2018-07-09 | Systems and methods of treating water used for hydraulic fracturing |
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US14/106,052 Expired - Fee Related US9358517B2 (en) | 2012-09-07 | 2013-12-13 | Systems and methods of treating water used for hydraulic fracturing |
US15/150,228 Expired - Fee Related US10040046B2 (en) | 2012-09-07 | 2016-05-09 | Systems and methods of treating water used for hydraulic fracturing |
US16/029,915 Abandoned US20180311634A1 (en) | 2012-09-07 | 2018-07-09 | Systems and methods of treating water used for hydraulic fracturing |
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US14/106,052 Expired - Fee Related US9358517B2 (en) | 2012-09-07 | 2013-12-13 | Systems and methods of treating water used for hydraulic fracturing |
US15/150,228 Expired - Fee Related US10040046B2 (en) | 2012-09-07 | 2016-05-09 | Systems and methods of treating water used for hydraulic fracturing |
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US20150060370A1 (en) * | 2013-09-03 | 2015-03-05 | Truox, Inc. | Chlorine dioxide generator for the efficient generation of chlorine dioxide in dilute solutions |
US9993758B2 (en) * | 2013-08-05 | 2018-06-12 | John J. Paoluccio | Closed antioxidant fluid system and method for promoting antioxidant properties thereof |
US10404823B2 (en) * | 2016-05-27 | 2019-09-03 | Home Box Office, Inc. | Multitier cache framework |
WO2018200710A2 (en) * | 2017-04-25 | 2018-11-01 | Hk Ip Llc | Compositions and methods for enhancing oil and/or gas production from water-contaminated wells |
US11572296B1 (en) | 2020-04-02 | 2023-02-07 | Bio-Cide International, Inc. | Method for extending time of activity of chlorite-based biocides |
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US6949196B2 (en) * | 2003-07-28 | 2005-09-27 | Fkos, Llc | Methods and systems for improved dosing of a chemical treatment, such as chlorine dioxide, into a fluid stream, such as a wastewater stream |
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- 2013-12-13 US US14/106,052 patent/US9358517B2/en not_active Expired - Fee Related
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US4945992A (en) * | 1986-12-22 | 1990-08-07 | Sacco Frank J | Process for producing or cleaning high pressure water injection wells |
US20070199904A1 (en) * | 2006-02-27 | 2007-08-30 | Jonathan Thompson | Methods for treatment of organic matter in liquid |
US20100006513A1 (en) * | 2006-08-03 | 2010-01-14 | Bromine Compounds Ltd. | Method, device and system for water treatment |
US20110132815A1 (en) * | 2010-04-09 | 2011-06-09 | Angelilli Jerome F | Portable Water Treatment System and Apparatus |
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US10040046B2 (en) | 2018-08-07 |
US9358517B2 (en) | 2016-06-07 |
US8962534B2 (en) | 2015-02-24 |
US20140072656A1 (en) | 2014-03-13 |
US20160251566A1 (en) | 2016-09-01 |
US20140100143A1 (en) | 2014-04-10 |
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