System and method for treatment of produced waters
The systems and methods disclosed herein process produced/flowback water, such as high total dissolved solids produced water, to generate high purity, high value products with little to no waste. The generated high purity, high value products include caustic soda, hydrochloric acid, and/or sodium hypochlorite. Further, the methods and systems disclosed herein generate high quality brine for electrolysis through the systematic removal of contaminants such as but not limited to suspended solids, iron, sulfides, barium, radium, strontium, calcium, magnesium, manganese, fluoride, heavy metals, organic carbon, recoverable hydrocarbons, silica, lithium, and/or nitrogen containing compounds. Further, some products generated by the systems and methods disclosed herein may be recovered and reutilized or sold for other uses, such as carbon dioxide, calcium oxide, chlorine, magnesium oxide, calcium carbonate, and/or barium sulfate.
1. A system for treating contaminated water to produce at least one of sodium hydroxide, hydrochloric acid, and sodium hypochlorite comprises:
a coagulation tank that oxidizes and coagulates effluent from waste water influent;
a first pH adjustment tank that adjusts a pH of effluent from the coagulation tank and is downstream of the coagulation tank;
a first floc mix tank that adds a first flocculant to effluent from the first pH adjustment tank and is located downstream of the first pH adjustment tank;
an iron clarifier that separates iron from effluent from the first floc mix tank and is located downstream of the first floc mix tank;
at least one multimedia filter that filters effluent from the iron clarifier and is located downstream of the iron clarifier;
a first organics removal system that removes at least petroleum hydrocarbons from effluent from the at least one multimedia filter and is located downstream of the at least one multimedia filter;
a second pH adjustment tank that adjusts the pH of effluent from the first organics removal system and is located downstream of the first organics removal system;
a softening clarifier that removes calcium carbonate and magnesium hydroxide sludge from effluent from the second pH adjustment tank and is located downstream of the second pH adjustment tank;
a third pH adjustment tank that adjusts the pH of effluent from the softening clarifier and is located downstream of the softening clarifier;
a filter that removes colloidal solids from effluent from the third pH adjustment tank and is located downstream of the third pH adjustment tank;
a second organics removal system that removes at least alcohol and ammonia from effluent from the filter and is located downstream of the first organics removal system;
an evaporative brine concentrator that concentrates effluent from the second organics removal system, wherein effluent from the evaporative brine concentrator is a concentrated purified brine and is located downstream of the second organics removal system;
a weak acid cation ion exchange column and a first chelating ion exchange column that removes any remaining calcium and remaining magnesium to a level of less than 50 ppb from effluent from the evaporative brine concentrator and is located downstream of the evaporative brine concentrator;
a reduction tank that depresses the pH and reduces bromate and iodate in effluent from the first chelating ion exchange column and is located downstream of the weak acid cation exchange column;
a third organics removal system that removes at least organic acid from effluent from the reduction tank and is located downstream of the reduction tank;
a fourth pH adjustment tank that adjusts the pH of effluent from the third organics removal system and is located downstream of the third organics removal system;
a second chelating ion exchange column that removes trace metals from effluent from the fourth pH adjustment tank and is located downstream of the fourth pH adjustment tank;
a fifth pH adjustment tank that adjusts the pH of effluent from the second chelating ion exchange column and is located downstream of the second chelating ion exchange column;
a bromine oxidation tank that removes bromine and iodine from effluent from the fifth pH adjustment tank and is located downstream of the fifth pH adjustment tank;
a sixth pH adjustment tank that adjusts the pH of effluent from the second chelating ion exchange column and is located downstream of the bromine oxidation tank; and
at least one electrolysis unit that converts the concentrated purified brine into at least one of sodium hydroxide, hydrochloric acid, and sodium hypochlorite and is located downstream of the sixth pH adjustment tank.
2. The system of claim 1 , further comprising:
a waste water screening device that removes grit and particulates from the waste water influent before the coagulation tank; and
at least one first equalization tank that equalizes flow and concentration of the effluent from the waste water screening device before the coagulation tank.
3. The system of claim 1 , wherein the reduction tank depresses the pH to give the effluent from the reduction tank a pH of less than 2,
wherein the third organics removal system is coconut shell activated carbon.
4. The system of claim 1 , further comprising:
a barium removal system that removes barium sulfate and strontium sulfate from effluent from the first organics removal system.
5. The system of claim 1 , wherein the softening clarifier further removes strontium sulfate from the effluent from the second pH adjustment tank.
6. The system of claim 1 , wherein the system for treating contaminated water further produces at least one of chlorine gas and iron chloride.
7. The system of claim 1 , wherein the first organics removal system is at least one of an organo-clay system and a resin bed.
8. The system of claim 1 , wherein the second organics removal system includes a distillation tower.
9. The system of claim 1 , wherein the effluent from the second organics removal system has an ammonia concentration of less than 1 mg/l,
wherein the first organics removal system produces water with a total organic content of less than 140 mg/l and removes over 99% of BTEX,
wherein the softening clarifier removes total metals to levels below 100 ppb, and
wherein the third organics removal system produces water with the total organic content of 10 mg/l or less.
10. The system of claim 1 , wherein the first pH adjustment tank adjusts the pH to a pH from 6.5 to 7.5,
wherein the second pH adjustment tank adjusts the pH to a pH from 10.5 to 12.5,
wherein the third pH adjustment tank adjusts the pH to a pH of at least 10.5,
wherein the reduction tank adjusts the pH to a pH of less than 2,
wherein the fourth pH adjustment tank adjusts the pH to a pH less than 4,
wherein the fifth pH adjustment tank adjusts the pH to a pH of 3 or less,
wherein the sixth pH adjustment tank adjusts the pH to a pH from 6 to 11.
11. A method for producing at least one of sodium hydroxide, hydrochloric acid, and sodium hypochlorite from contaminated water comprises:
removing iron from influent water to produce an iron reduced effluent;
removing petroleum hydrocarbons from the iron reduced effluent to produce a petroleum hydrocarbon reduced effluent;
removing at least one of calcium and magnesium from the petroleum hydrocarbon reduced effluent to produce a softened effluent;
removing at least alcohol and ammonia from the softened effluent to produce an alcohol and ammonia reduced brine;
evaporating the alcohol and ammonia reduced brine to produce a concentrated brine;
removing at least organic acid from the concentrated brine to produce an organic acid reduced brine;
removing iodine and bromine species from the organic acid reduced brine to produce a polished brine; and
treating the polished brine with electrolysis to produce at least one of sodium hydroxide, hydrochloric acid, and sodium hypochlorite.
12. The method of claim 11 , wherein the step of treating the concentrated brine with the electrolysis further produces chlorine gas.
13. The method of claim 12 , further comprising:
processing the chlorine gas to produce iron chloride.
14. The method of claim 11 , wherein the step of removing at least one of the calcium and the magnesium from the petroleum hydrocarbon reduced effluent additionally removes fluoride from the petroleum hydrocarbon reduced effluent.
15. The method of claim 11 , further comprising:
removing barium and strontium from the petroleum hydrocarbon reduced effluent before performing the step of removing at least one of the calcium and the magnesium.
16. The method of claim 11 , wherein the step of removing at least one of the calcium and the magnesium from the petroleum hydrocarbon reduced effluent additionally removes strontium from the petroleum hydrocarbon reduced effluent.
17. The method of claim 11 , wherein the step of removing at least the organic acid from the concentrated brine includes depressing the concentrated brine to a pH of less than two to form a pH depressed concentrated brine and then treating the pH depressed concentrated brine with activated carbon made from coconut shells.
18. The method of claim 11 , wherein the step of removing the petroleum hydrocarbons includes treating influent water with a dissolved air floatation device and treating the iron reduced effluent with a at least one of a resin bed and an organo-clay system, and
wherein the step of removing at least the alcohol and ammonia includes treating the softened effluent with a distillation tower.
19. A system for treating contaminated water to produce at least one of sodium hydroxide, hydrochloric acid, and sodium hypochlorite comprises:
a separated solids and iron removal system;
a first organics removal system that removes at least petroleum hydrocarbons located downstream of the separated solids and iron removal system;
a soda softening system located downstream of the first organics removal;
a second organics removal system that removes alcohol and ammonia and that is located upstream of a brine evaporation system and downstream from the first organics removal system;
the brine evaporation system located downstream of the soda softening system and the second organics removal system;
a third organics removal system that removes at least organic acid located downstream of the brine evaporation system; and
an electrolysis system located downstream of the third organics removal system,
wherein the system is configured to produce at least one of sodium hydroxide, hydrochloric acid, and sodium hypochlorite.