US2014332391A1PendingUtilityA1

Fracture Water Treatment Method and System

Assignee: MBJ Water PartnersPriority: Jul 27, 2012Filed: Jul 23, 2014Published: Nov 13, 2014
Est. expiryJul 27, 2032(~6 yrs left)· nominal 20-yr term from priority
E21B 43/267C02F 2103/06C02F 1/484C02F 2209/02C02F 1/008C02F 2103/10B01D 21/2494B01D 19/00B01D 21/34B01D 19/0063C02F 2209/42B01D 17/12B01D 19/0068B01D 21/0009C02F 2101/32B01D 21/10E21B 21/065B01D 17/04B01D 17/0208B01D 21/24C02F 2209/005B01D 17/0214C02F 2201/483C02F 1/487E21B 43/35E21B 43/2607
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Claims

Abstract

A method and system for treatment of flow-back and produced water from a hydrocarbon well in which fracturing operations are carried out using a phase separation and creating of positive charge in the water.

Claims

exact text as granted — not AI-modified
1 - 9 . (canceled) 
     
     
         10 . A system for treating hydrocarbon well fracture water from a hydrocarbon well, a system comprising:
 means for separating solids from fracture water, wherein a flow of water with suspended solids results;   means for separating the flow of water into a plurality of flows of water;   means for generating positive charge in the plurality of flows of water, wherein a plurality of flows of positively-charged water results; and   means for comingling plurality of flows of positively-charged water.   
     
     
         11 . A system as in  claim 10 , wherein said means for separating comprises a three-phase, four material separator. 
     
     
         12 . A system as in  claim 11 , wherein said means for separating further comprises a second two phase separator, the two-phase separator comprising an input for receiving water flow from the three-phase gas oil separator, and an output for the flow f water with suspended solids. 
     
     
         13 . A system as in  claim 11 , further comprising:
 means for monitoring an oil/water interface level; and   means for controlling the oil/water interface level in the first and second separator.   
     
     
         14 . A system as in  claim 10 , wherein the means for separating the flow of water into a plurality of flows of water comprises a manifold having an input port to receive the flow of water with suspended solids and a plurality of output ports, each of which has a cross-sectional area that is smaller than the cross-sectional area of the input of the manifold; and
 wherein the sum of the cross-sectional areas of the output ports is greater than the cross-sectional area of the input ports, whereby the flow rate exiting the manifold is less than the flow rate entering the manifold.   
     
     
         15 . A system as in  claim 10 , wherein the means for separating the flow of water into a plurality of flows of water comprises a water truck having a plurality of compartments, each compartment being positioned to receive a portion of the flow of water. 
     
     
         16 . A system as in  claim 10 , wherein said means for generating positive charge comprises means for treating each of the plurality of flows of water with electromagnetic flux. 
     
     
         17 . A system as in  claim 16 , wherein the means for treating each of the plurality of flows of water with electromagnetic flux comprises:
 a pipe; and   at least one electrical coil having an axis substantially coaxial with the pipe.   
     
     
         18 . A system as in  claim 10 , wherein said means for co-mingling comprises a manifold having input ports for a plurality of flows of positively-charged water and an output port. 
     
     
         19 . A system as in  claim 18 , wherein said means for co-mingling further comprises a well fracturing water and proppant blender. 
     
     
         20 . A system as in  claim 10 , wherein the majority of the suspended solids are less than about 100 microns. 
     
     
         21 . A system as in  claim 20 , wherein substantially all the suspended solids are less than about 100 microns. 
     
     
         22 . A system as in  claim 21 , wherein the majority of the suspended solids are less than about 10 microns. 
     
     
         23 . A system as in  claim 10 , wherein said means for separating comprises a two-stage separator. 
     
     
         24 . A system as in  claim 23 , wherein said two-stage separator comprises:
 a three-phase separator having a water output coupled to an input of a two-phase separator.   
     
     
         25 - 30 . (canceled)

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