Apparatuses, systems and methods for efficient solubilization of carbon dioxide in water using high energy impact

Abstract

A method for the efficient solubilization of carbon dioxide in water through the use of high energy impacts is disclosed. The method can optionally includes mixing the carbon dioxide and water to form an annular dispersed flow, accelerating the carbon dioxide and water prior to the collision; providing a retention network to collect the carbonated water flow. Also disclosed are systems and apparatuses for practicing the disclosed methods.

1 - 11 . (canceled) 
     
     
         12 . An apparatus for the solubilization of carbon dioxide in water comprising:
 a conduit defining a flow path;   an inlet manifold on the proximal end of the conduit, the inlet manifold having a first branch for receiving water and a second branch for receiving carbon dioxide;   one or more dispersion elements arranged within the conduit;   a passive accelerator within the conduit;   a rigid impact surface, positioned downstream of the passive accelerator; and   a retention network coupled to the distal end of the conduit,   wherein the conduit, passive accelerator, and rigid impact surface are configured with respect to one another such that impact of a flow passing through the conduit at between about 0.1 to about 3.7 gallons per minutes results in pressure energy densities at the rigid impact surface of between about −40 foot-pound/cm 3  to 5 foot-pound/cm 3 .   
     
     
         13 . The apparatus of  claim 12  where the inlet manifold comprises a Y-shaped connector with a carbon dioxide supply on one branch of the Y-shaped inlet and a water supply on the other branch of the Y-shaped inlet. 
     
     
         14 . The apparatus of  claim 12  where the dispersion elements comprise at least one of static helical mixers and static directional mixers. 
     
     
         15 . (canceled) 
     
     
         16 . (canceled) 
     
     
         17 . The apparatus of  claim 12  where the passive accelerator comprises a cylindrical orifice. 
     
     
         18 . The apparatus of  claim 12  where the passive accelerator comprises an hourglass shaped nozzle. 
     
     
         19 . (canceled) 
     
     
         20 . (canceled) 
     
     
         21 . The apparatus of  claim 12  where the retention network comprises static mixers. 
     
     
         22 . (canceled) 
     
     
         23 . (canceled) 
     
     
         24 . The apparatus of  claim 12  wherein a ratio of the cross sectional area of a portion of the conduit immediately preceding the passive accelerator compared to the cross sectional area of a restriction within the passive accelerator is such that the it will accelerate the speed of a fluid flow within the conduit up to 100 times. 
     
     
         25 . (canceled) 
     
     
         26 . (canceled) 
     
     
         27 . The apparatus of  claim 12 , wherein the rigid impact surface is oriented substantially normal to the flow path through the conduit at an outlet of the passive accelerator and an output opening of the passive accelerator is configured such that a straight line projection from each point in the output opening along a longitudinal axis of the conduit intersects the rigid impact surface. 
     
     
         28 . The apparatus of  claim 12 , wherein the rigid impact surface is positioned between about 0.1 to about 2.0 inches downstream from the passive accelerator. 
     
     
         29 . The apparatus of the  claim 12 , wherein the passive accelerator comprises a contraction or converging restriction having an energy loss coefficient in the range of about 0.1 to about 0.44. 
     
     
         30 . The apparatus of  claim 12 , wherein the dispersion element, the conduit, and the passive accelerator are substantially aligned along a central longitudinal axis. 
     
     
         31 . The apparatus of  claim 30 , wherein the rigid impact surface defines at least one peripheral flow path offset from the central longitudinal axis in direction transverse to the central longitudinal axis. 
     
     
         32 . The apparatus of  claim 30 , wherein the retention network includes a second helical dispersion element aligned with the longitudinal axis. 
     
     
         33 . An apparatus for the solubilization of carbon dioxide in water comprising:
 a tubular conduit disposed about a longitudinal axis, extending from an input end to and output end, and defining a fluid flow path from the input end to the output end;   an inlet manifold comprising a first inlet for water, a second inlet for carbon dioxide, and an outlet in fluid communication with the input end of the conduit;   a passive accelerator located within the conduit, the passive accelerator comprising a restriction of the conduit having a reduced cross sectional area relative to portions of the conduit immediately upstream and downstream of the restriction portion; and   a rigid impact surface downstream positioned about 0.1 and about 2.0 inches downstream of the passive accelerator and filling a central portion of the conduit and defining one or more peripheral flow paths located outside of the central portion of the tubular conduit; wherein:
 the tubular conduit and restriction portion are substantially aligned along a longitudinal axis, and the peripheral flow paths are offset from the central longitudinal axis in a direction transverse to the central longitudinal axis, and 
 the passive accelerator has an output opening having a radial size that is less than the radial extent of the central portion of the conduit filled by the rigid impact surface. 
   
     
     
         34 . The apparatus of  claim 33 , wherein the conduit, passive accelerator, and rigid impact surface are configured with respect to one another such that impact of a flow passing through the conduit at between about 0.1 to about 3.7 gallons per minutes results in pressure energy densities at the rigid impact surface of between about −40 foot-pound/cm 3  to 5 foot-pound/cm 3 . 
     
     
         35 . The apparatus of  claim 34 , where the inlet manifold comprises a Y-shaped connector with a carbon dioxide supply on one branch of the Y-shaped inlet and a water supply on the other branch of the Y-shaped inlet. 
     
     
         36 . The apparatus of  claim 33  where the dispersion elements comprise at least one of static helical mixers and static directional mixers. 
     
     
         37 . The apparatus of  claim 33  where the passive accelerator comprises a cylindrical orifice. 
     
     
         38 . The apparatus of  claim 33  where the passive accelerator comprises an hourglass shaped nozzle. 
     
     
         39 . The apparatus of  claim 33  where the retention network comprises static mixers. 
     
     
         40 . The apparatus of  claim 33  wherein a ratio of the cross sectional area of a portion of the conduit immediately preceding the passive accelerator compared to the cross sectional area of a restriction within the passive accelerator is such that it will accelerate the speed of a fluid flow within the conduit up to 100 times. 
     
     
         41 . The apparatus of  claim 33 , wherein the rigid impact surface is oriented substantially normal to the flow path through the conduit at an outlet of the passive accelerator and an output opening of the passive accelerator is configured such that a straight line projection from each point in the output opening along a longitudinal axis of the conduit intersects the rigid impact surface. 
     
     
         42 . The apparatus of the  claim 33 , wherein the passive accelerator comprises a contraction or converging restriction having an energy loss coefficient in the range of about 0.1 to about 0.44.