Abstract:
Portable disposable wastewater recycling techniques and systems are provided. Waste water returning to the surface during the process of hydraulic fracking or mining is routed through a portable water filtration system to remove impurities on site and to eject clean portable environmental safe water.

Description:
BACKGROUND 
       [0001]    Hydraulic fracturing (fracking) is one of the mining and natural oil and gas exploration activities that generate large volumes of waste water (flow back) during the initial drilling process. Somewhere between 20-40% of the water used for fracking a well returns to the surface as wastewater. A typical fracking well will consume between 3-5 million gallons of water during the fracking process, with 500,000-1,200,000 gallons returning to the surface as contaminated flow back water. The contaminants within the flow back water consists of the drilling additives (surfactants, biocides, gelling agents and propants) required to optimize the drilling process. There are organic pollutants such as benzene, toluene, xylenes, diesel range and gasoline range organics which are resultant of injected chemicals and from natural sources. Soluble salts of sodium and calcium make up as much as 10-20% of the flow back water. Traditional methods of recovery of these contaminants are to build a recovery pond on site and allow the particulate matter to settle out of the water. The clear water is transported by truck to the nearest water treatment facility or to a deep-well injection site to be disposed of. Due to the salty brine content of the wastewater, most wastewater treatment plants cannot treat salty wastewater because they use a biological treatment where freshwater microbes clean the water. High levels of salt and total dissolved solids (TDS) could harm the process if all of a sudden the water taken in is salty, it could kill the microbes. Deep-well injection of the wastewater has issues with shallow drinking water aquifer contamination from the injection into non stable rock strata allowing upward migration of contaminated water. 
         [0002]    Therefore, there is a need for a portable waste removal system that can remove the suspended solids, extract the organic compounds and absorb the soluble salts, especially sodium and calcium while generating clean water for immediate recycled use on site at the high volume rates required in the fracking process. 
       SUMMARY 
       [0003]    In various embodiments, techniques, apparatuses, and systems for portable wastewater recycling are presented. According to an embodiment, a portable wastewater disposable recycling is provided. 
     
    
     
       BRIEF DESCRIPTION OF THE DRAWINGS 
         [0004]      FIG. 1  is an exploded perspective view of one embodiment of a filtration bag constructed, according to an example embodiment. 
           [0005]      FIG. 2  is a bottom plan view of the filtration bag of the  FIG. 1 , according to an example embodiment. 
           [0006]      FIG. 3  is a diagrammatic view through the center of the water disposal system of the  FIG. 1  when the system is partially exposed, according to an example embodiment. 
           [0007]      FIG. 4  is a process flow chart showing the processing path of wastewater and the filtration steps during the filtration to complete purification into potable water, according to an example embodiment. 
           [0008]      FIG. 5  is a diagrammatic view through the center of the containment cage in the erect position or condition, according to an example embodiment. 
           [0009]      FIG. 6  is a diagrammatic view of the locking assembly of the containment cage to lock it in the erect position or condition, according to an example embodiment. 
           [0010]      FIG. 7  is a diagrammatic view of the portable trailer assembly of filter bags, according to an example embodiment. 
           [0011]      FIG. 8  is a view of the containment cage in an unlocked and unfolded position or condition, according to an example embodiment. 
       
    
    
     DETAILED DESCRIPTION 
       [0012]    With initial reference to the  FIGS. 1-3 ; it is illustrated that in one embodiment of the filtration bag ( 8 ) the oil fracking wastewater ( 22 ) (see  FIG. 3 ) is pumped into the filtration bag ( 8 ) through the bag collar( 14 ) and separated into its solid and liquid phase with the help of a flocculating agent ( 21 ) (see  FIG. 3 ). The solid phase ( 19 ) (see  FIG. 3 ) is retained in filtration bag ( 8 ) via the 50 um and 25 um ( 20  &amp;  18 ) respectively (see  FIG. 3 ) non-woven filter materials. The liquid phase ( 24 ) (see  FIG. 3 ) is allowed to pass through filter media ( 20  &amp;  18 ) through the woven perforated outer skin media ( 13 ) (see  FIG. 3 ). In one embodiment, the filtration bag ( 8 ) is a 3 ply bag (see  FIG. 3 ). The filtration bag ( 8 ) has a top ( 25 ) with an opening ( 14 ) surrounded by a neck ( 27 ), a top ( 25 ), a bottom ( 28 ) (see  FIG. 2 ) and four sides ( 26 ) of the same dimensions. In one embodiment the filtration bag ( 8 ) has external support straps ( 12 ) and ( 9  &amp; 11 ) for additional strength. The opening ( 14 ) has a diameter of 12 inches. The inner-two plys ( 18  &amp;  20 ) of the filtration bags ( 8 ) are approximately 42 inches square consisting of the bottom ( 28 ) (see  FIG. 2 ), 4 sides ( 26 ) and top ( 25 ). All seams are sewn or otherwise secured around exterior edges, corners to exterior ply ( 26 ) of filtration bag ( 8 ). Other size filtration cloths may be used dependent on desired filtrate needs. In one preferred embodiment, the filtration bag ( 8 ), the exterior ply ( 26 ) is made of woven polypropylene for strength and has perforations ( 13 ) cut into ply for drainage of liquid phase ( 23 ) of filtration. Both filtration media ( 20  &amp;  18 ) along with exterior skin ( 26 ) are constructed of non-woven and woven polypropylene respectively, but may be made of any suitable material. In an embodiment of the invention the filtration bag ( 8 ) has two lifting straps ( 14  &amp;  15 ) each being formed into a lifting loop ( 16  &amp;  17 ) at the top of the filtration bag ( 8 ). These straps extend down the sides or corners of the exterior ply ( 26 ) of the filtration bag ( 8 ) and form an X pattern at the bottom of the filtration bag (see  FIG. 2 ). There are also reinforcing straps  9 ,  11 ,  10  &amp;  12  sewn onto the outer ply ( 26 ) and these straps are made of woven polypropylene. The lifting straps ( 14  &amp;  15 ) are designed to lift 4,000 lbs. of weight. 
         [0013]    According to an embodiment, the filtration bag ( 8 ) is 42 inches in length, 42 inches in width, 42 inches in height. However, another size or configuration of filtration bag may be used without departing from the teachings discussed herein. 
         [0014]    With reference now to the  FIGS. 4-8 , it is demonstrated that the waste filtration bags ( 8 ) utilizes collapsible wire cage or bag support ( 29 ) shown in erected position. In the  FIG. 8 , this cage is shown in a fully collapsed position. As best illustrated in the  FIG. 5 , the wire cage ( 29 ) comprises a welded wire grid base or bottom panel ( 31 ) having front and rear border rods or wires pivotally connected by helical lacing wires ( 32 ) to a welded wire front panel ( 33 ) and a rear panel ( 34 ) respectively. Each of the front panel ( 33 ) and a rear panel ( 34 ) also comprise a welded wire grid. This rear panel ( 34 ) has edge-most border rods or wires helically laced to edge-most rods or wires of side panels ( 35 ,  36 ) such that the side panels ( 35 ,  36 ) may be pivoted relative to the back or rear panel ( 34 ). As may be seen most clearly in the  FIG. 8  when the wire cage is collapsed, the front panel ( 33 ) is pivoted downwardly into contact with the top surface of the bottom panel ( 31 ). The side panels ( 35 ,  36 ) are pivoted inwardly one atop the other, and onto back panel ( 34 ) then pivoted onto the top of the collapsed front and side panels to create a fully collapsible cage. Other methods of collapsing the wire cage ( 29 ) may be used as desired. 
         [0015]    In the illustrated embodiment, there are feet ( 38 ) attached to the underside of the bottom panel ( 37 ) at the four corners of the panel ( 31 ). These feet may be welded or otherwise secured to the underside of the bottom panel ( 31 ) and, in turn, may be secured to a conventional wooden pallet or the bed of a truck for transportation from one site to another. 
         [0016]    With reference to the  FIG. 6 , it is illustrated that there are four locking mechanisms, two on each side of front panel ( 33 ) which function to help maintain the cage ( 29 ) in its erect condition. These locking mechanisms ( 38 ) cooperate with loops ( 39 ) on the front edges ( 40 ) of the side panels ( 35 ,  36 ) to secure the cage ( 29 ) in an erect position or condition. Although two locking mechanisms ( 38 ) are shown on each side of the front panel ( 29 ), it will be understood by those skilled in the art that any number of locking mechanisms of any known configuration or type may be used in accordance with the present invention. 
         [0017]    With reference to the  FIGS. 4 and 7 , it is illustrated that the filtration bag ( 8 ), cages ( 29 ) are mounted in a mobile trailer ( 41 ). The wastewater is pumped from the well to the inlet connection ( 45 ) (which extends through container wall  42  and onto pneumatic valve  43  having an in-line inductor  46 ). The wastewater travels through pipe ( 44 ) to discharge hoses ( 50 ) into each filter bag ( 8 ). The suspended solids are removed via gravity feed through filter bags ( 8 ) and collects in water tight container having a flock agent  21 , a check valve  47 , pneumatic pump  48 , and traveling via 1 inch diameter hose  49  (see the  FIG. 4 ). Pneumatic pump ( 51 ) transfers filtrate through valve  52  along flexible  1  and a half inch hose  53  to activate carbon filter ( 54 ) to remove organic compounds. Filtrate is further transferred to cation/anion bead filtration tanks ( 55 ) to remove soluble calcium chloride and sodium chloride. Clean potable water leaves trailer via exit connection ( 57 ) after passing through water meter  56 . All suspended solids contained in filter bag ( 8 ), organic contaminants contained in activate carbon filter ( 54 ) and soluble salts contained in cation/anion filter ( 55 ) to be removed from site for proper disposal. Clean potable water to be recycled in well head. 
         [0018]    It is noted that any type of water filtration is intended to be included herein. So, a desalinization and a reverse osmosis process can be used without departing from the embodiments presented herein and above. 
         [0019]    The above description is illustrative, and not restrictive. Many other embodiments will be apparent to those of skill in the art upon reviewing the above description. The scope of embodiments should therefore be determined with reference to the appended claims, along with the full scope of equivalents to which such claims are entitled. 
         [0020]    The Abstract is provided to comply with 37 C.F.R. §1.72(b) and will allow the reader to quickly ascertain the nature and gist of the technical disclosure. It is submitted with the understanding that it will not be used to interpret or limit the scope or meaning of the claims. 
         [0021]    In the foregoing description of the embodiments, various features are grouped together in a single embodiment for the purpose of streamlining the disclosure. This method of disclosure is not to be interpreted as reflecting that the claimed embodiments have more features than are expressly recited in each claim. Rather, as the following claims reflect, inventive subject matter lies in less than all features of a single disclosed embodiment. Thus the following claims are hereby incorporated into the Description of the Embodiments, with each claim standing on its own as a separate exemplary embodiment.