REMOVAL OF SELENIUM FROM COAL MINE WASTEWATER
20170341960 ยท 2017-11-30
Inventors
Cpc classification
C02F1/5245
CHEMISTRY; METALLURGY
International classification
Abstract
A system, a method and a process is provided for removing selenium from coal mine wastewater. The method and system include the steps of providing a quantity of ferric chloride in a predetermined relative ratio to a volume of mine wastewater, using sodium hydroxide to adjust the pH of the mine wastewater between 7.5 and 8, introducing the volume of mine wastewater into a sediment pond or tank having turbidity curtains.
Claims
1-2. (canceled)
3. A method for removing selenium from wastewater comprising: providing a quantity of ferric chloride in a predetermined relative ratio to a volume of wastewater; adjusting a pH of the volume of wastewater; and introducing the volume of wastewater into a vessel.
4. The method of claim 1, wherein the adjusting of the pH is achieved by adding sodium hydroxide to the mine wastewater.
5. The method of claim 2, wherein the pH is adjusted to a slightly alkaline value.
6. The method of claim 3, wherein the pH value is in the range of 7.5 to 8.
7. The method of claim 1, wherein the wastewater vessel is a sediment pond.
8. The method of claim 1, wherein the wastewater vessel is a tank.
9. The method of claim 1, further comprising receiving the wastewater from a coal mine discharge location.
10. The method of claim 1, wherein the wastewater volume is held in a pond or tank.
11. The method of claim 8, further comprising providing turbidity curtains in the pond or tank.
12. A system for removing selenium from wastewater including: means for determining a concentration ratio of ferric chloride; means for introducing the determined amount of ferric chloride into a volume of wastewater; a vessel for storing the volume of wastewater, and means for discharging the wastewater after treatment.
13. The system of claim 10, wherein the concentration of ferric chloride is determined for a range of volumes of wastewater.
14. The system of claim 10, wherein the vessel comprises a plurality of turbidity curtains.
15. The system of claim 12, wherein the turbidity curtains comprise windows for flow of wastewater therethrough.
16. The system of claim 10, wherein the windows in the turbidity curtains are configured to achieve clarification of the wastewater and settling of solids in the wastewater.
17. A process for removing selenium from wastewater comprising: combining one or more chemical components in a predetermined proportion preparing a water treatment site by installing turbidity curtains in a retention pond; providing a predetermined volume of wastewater in the retention pond; cleaning the retention pond; providing a quantity of ferric chloride and a quantity of sodium hydroxide; and mixing a predetermined quantity of ferric chloride with the wastewater to extract selenium in the mine wastewater
18. The process of claim 15, further comprising adding sodium hydroxide to the wastewater
19. The process of claim 16, further comprising adjusting the pH of the volume of wastewater.
20. The process of claim 17, wherein the pH of the volume of wastewater is adjusted to a pH value in the range of 7.5 to 8.
21. The process of claim 15, wherein the quantity of the ferric chloride and the quantity of sodium hydroxide are determined, respectively, on field testing and measurements of selenium concentration in the wastewater.
22. The process of claim 19, wherein the field testing and measurements of selenium is determined at the location of mine wastewater discharge and collection sites.
Description
BRIEF DESCRIPTION OF THE FIGURES
[0009] The application will become more fully understood from the following detailed description, taken in conjunction with the accompanying FIGURES, wherein like reference numerals refer to like elements, in which:
[0010]
DETAILED DESCRIPTION OF THE EXEMPLARY EMBODIMENTS
[0011] Before turning to the FIGURES which illustrate the exemplary embodiments in detail, it should be understood that the application is not limited to the details or methodology set forth in the following description or illustrated in the FIGURES.
[0012] Referring to
[0013] At step 112 a receiving sediment structure is constructed with sufficient depth to store the resultant sludge. The sediment structure may be equipped with turbidity curtains with windows to produce clarified water that can be discharged, e.g., via pumps, drainpipes, and conventional water discharge equipment, into receiving streams. If all of the conditions set for the above are met, in practice compliance limits with selenium may be achieved. At step 114 the treated mine wastewater discharge is sampled for analysis.
[0014] It should also be understood that the phraseology and terminology employed herein is for the purpose of description only and should not be regarded as limiting. While the exemplary embodiments illustrated in the figures and described herein are presently preferred, it should be understood that these embodiments are offered by way of example only. Accordingly, the present application is not limited to a particular embodiment, but extends to various modifications that nevertheless fall within the scope of the appended claims. The order or sequence of any processes or method steps may be varied or re-sequenced according to alternative embodiments.
[0015] It should be noted that although the FIGURES or written description herein may disclose a specific order of method steps, it is understood that the order of these steps may differ from what is depicted. Also two or more steps may be performed concurrently or with partial concurrence. Such variation will depend on the software and hardware systems chosen and on designer choice. It is understood that all such variations are within the scope of the application.