Scale control in oilfield produced waters

Abstract

Systems and methods include scale control in oilfield produced waters. Thermodynamic data indicative of surface conditions and subterranean conditions of a subterranean region including a well is received, from probes. An acidity of a produced water stream to be disposed in the well is received from a pH meter. A supersaturation degree of the produced water stream to be disposed in the well is determined, by using the thermodynamic data. An amount of carbon dioxide to be injected in the produced water stream to neutralize a scaling risk is determined, by the one or more processors, by using the supersaturation degree and the acidity. An injection of the amount of the carbon dioxide in the produced water stream is triggered to neutralize the scaling risk.

What is claimed is: 
     
         1 . A computer-implemented system comprising:
 memory storing application programming interface information; and   a server performing operations comprising:
 receiving, by one or more processors from probes, thermodynamic data indicative of surface conditions and subterranean conditions of a subterranean region comprising a well; 
 receiving, by the one or more processors from a pH meter, an acidity of a produced water stream to be disposed in the well; 
 determining, by the one or more processors, by using the thermodynamic data, a supersaturation degree of the produced water stream to be disposed in the well; 
 determining, by the one or more processors, by using the supersaturation degree and the acidity, an amount of carbon dioxide to be injected in the produced water stream to neutralize a scaling risk; and 
 triggering, by the one or more processors, an injection of the amount of the carbon dioxide in the produced water stream to neutralize the scaling risk. 
   
     
     
         2 . The computer-implemented system of  claim 1 , wherein determining the supersaturation degree of the produced water stream comprises determining a saturation ratio of the produced water stream. 
     
     
         3 . The computer-implemented system of  claim 1 , wherein probe data comprises temperature, pressure data, and flow data. 
     
     
         4 . The computer-implemented system of  claim 1 , wherein the pH meter is located at least about 60 meters after a mixture point. 
     
     
         5 . The computer-implemented system of  claim 1 , wherein the scaling risk comprises formation of calcium carbonate. 
     
     
         6 . The computer-implemented system of  claim 1 , wherein the amount of the carbon dioxide is injected in the produced water stream in a liquid phase or a supercritical phase. 
     
     
         7 . The computer-implemented system of  claim 1 , wherein the produced water stream is filtered to remove oil and heavy particles. 
     
     
         8 . The computer-implemented system of  claim 1 , wherein the produced water stream comprises ion components comprising sodium (Na + ), chloride (Cl − ), calcium (Ca 2+ ), magnesium (Mg 2+ ), bicarbonate (HCO 3− ), and sulfate (SO 4   2− ). 
     
     
         9 . A non-transitory computer-readable media encoded with a computer program, the computer program comprising instructions that when executed by one or more computers cause the one or more computers to perform operations comprising:
 receiving, by one or more processors from probes, thermodynamic data indicative of surface conditions and subterranean conditions of a subterranean region comprising a well;   receiving, by the one or more processors from a pH meter, an acidity of a produced water stream to be disposed in the well;   determining, by the one or more processors, by using the thermodynamic data, a supersaturation degree of the produced water stream to be disposed in the well;   determining, by the one or more processors, by using the supersaturation degree and the acidity, an amount of carbon dioxide to be injected in the produced water stream to neutralize a scaling risk; and   triggering, by the one or more processors, an injection of the amount of the carbon dioxide in the produced water stream to neutralize the scaling risk.   
     
     
         10 . The non-transitory computer-readable media of  claim 9 , wherein determining the supersaturation degree of the produced water stream comprises determining a saturation ratio of the produced water stream. 
     
     
         11 . The non-transitory computer-readable media of  claim 9 , wherein probe data comprises temperature, pressure data, and flow data, wherein the pH meter is located at least about 60 meters after a mixture point, wherein the scaling risk comprises formation of calcium carbonate, and wherein the amount of the carbon dioxide is injected in the produced water stream in a liquid phase or a supercritical phase. 
     
     
         12 . The non-transitory computer-readable media of  claim 9 , wherein the produced water stream is filtered to remove oil and heavy particles, and wherein the produced water stream comprises ion components comprising sodium (Na + ), chloride (Cl − ), calcium (Ca 2+ ), magnesium (Mg 2+ ), bicarbonate (HCO 3− ), and sulfate (SO 4   2− ).