System and method for removing iron from waste water
Systems and methods for removing iron from waste water employ one or more oxidizers, one or more treatment tanks having one or more self-generating and self-sustaining active sludge layers, and one or more spray-atomizing devices. A mixture of flowback fracturing water, or produced water, and the one or more oxidizers is spray-atomized by the spray-atomizing device inside the one or more treatment tanks. The atomized mixture settles in the one or more treatment tanks resulting in one or more self-generating and self-sustaining active sludge layers and one or more treated solutions. Additional mixtures of the flowback fracturing water, or produced water, and the one or more oxidizers may be continually spray-atomized into the one or more treatment tanks and filtered by the one or more sludge layer(s) so as to remove precipitated iron species from accumulated distillates and produce additional treated solutions for collection in one or more finish tanks.
1. A method for treating flowback fracturing water or produced water comprising:
adding an oxidizer to a first solution of flowback fracturing water or produced water to create a first mixture;
spray-atomizing the first mixture into a treatment tank causing a formation of a sludge layer on top of a formation of a treated solution forming in the treatment tank; and
spray-atomizing additional mixture into the treatment tank that includes at least the sludge layer, where the additional mixture, in response to the spray-atomizing the additional mixture, contacts and interacts with the sludge layer in the treatment tank, wherein the contacting and interacting causes iron species from the additional mixture to be absorbed into the sludge layer causing the production of additional treated solution and additional sludge in the sludge layer, wherein the sludge layer with the additional sludge is on top of the additional treated solution in the treatment.
2. The method of claim 1 further comprising:
pumping the treated solution and the additional treated solution to a finish tank;
wherein the sludge layer increases in volume based on the contacting and interacting.
3. The method of claim 1 further comprising maintaining the treatment tank at zero atmosphere during the spray-atomizing.
4. The method of claim 1 further comprising:
misting the first mixture into a second treatment tank, a third treatment tank and a fourth treatment tank;
settling the first mixture in the second, third and fourth treatment tanks, wherein a second sludge layer forms in the second treatment tank, a third sludge layer forms in the third treatment tank, and a fourth sludge layer forms in the fourth treatment tank in response to settling the mixture in the second, third and fourth treatment tanks;
filtering the mixture through the second, third, and fourth sludge layers; and
pumping a third treated solution, a fourth treated solution and a fifth treated solution to a finish tank.
5. The method of claim 4 further comprising:
interconnecting the treatment tank and the second treatment tank, the third treatment tank, and the fourth treatment tank with a belly line extending across and through a portion of each of the treatment tank, the second treatment tank, the third treatment tank, and the fourth treatment tank, the belly line having an start point and an end point;
running the treated solution, additional treated solution, the third treated solution, the fourth treated solution, and the fifth treated solution through the belly line from the start point to the end point; and
collecting the treated solution, the additional treated solution, the third treated solution, the fourth treated solution, and the fifth treated solution from the end point.
6. The method of claim 5 further comprising pumping the fourth treated solution and the fifth treated solutions out of tops of the third treatment tank and the fourth treatment tank.
7. The method of claim 1 further comprising a venting subsystem wherein gas or vapor is vented from the treatment tank to the venting subsystem.
8. The method of claim 1 further comprising:
pumping the treated solution from the treatment tank directly to one or more filters;
filtering the treated solution using the one or more filters; and
pumping the treated solution from the one or more filters directly to a finish tank.
9. The method of claim 1 wherein the oxidizer is one or more of a hypochlorite, ozone, oxygen, a chlorite, a permanganate, a peroxide, a persulfate, a perborate, a percarbonate, a N-halogenated hydantoin, chlorine dioxide, peracetic.
10. The method of claim 1 wherein the sludge layer is active, self-generating and self-sustaining.
11. The method of claim 10 further comprising maintaining the sludge layer at 8-10 m 3 .
12. The method of claim 1 wherein the at least one treatment tank is at least two treatment tanks and wherein forming the sludge layer and the treated solution is performed in either a batch sequence or a continuous sequence.
13. The method of claim 1 further comprising adding floatable material to the sludge layer.