US2009241525A1PendingUtilityA1

Systems, devices, and/or methods for recuperating energy and/or particulates

Assignee: NETTEK INTERNATPriority: Feb 18, 2008Filed: Jan 12, 2009Published: Oct 1, 2009
Est. expiryFeb 18, 2028(~1.6 yrs left)· nominal 20-yr term from priority
F01N 3/043F28C 3/06F01N 2240/02F28D 21/0003F28F 1/02F28D 7/106Y02T10/12F01N 5/02Y02P70/10B01D 47/06B01D 2247/04F28F 1/06F01N 3/04F28D 7/16
20
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Claims

Abstract

Certain exemplary embodiments provide an energy and particle recuperator (EPR) for dirty gas fluids and/or gas solids fluid mixes. Gas fluids and/or gas solids fluid mixes stream through a vessel. Heat contained in the gas fluids and/or gas solid fluid mixes is partially transferred to a liquid spray fluid sprayed inside the vessel. Heat is transferred from the liquid to a clean process fluid via a heat exchanger.

Claims

exact text as granted — not AI-modified
1 . A system, comprising:
 an energy and particle recuperator adapted to process a gas fluid, said energy and particle recuperator comprising a substantially hollow body, said substantially hollow body having a substantially cylindrical portion, said substantially cylindrical portion defining a central longitudinal axis, said energy and particle recuperator comprising a gas inlet, said central longitudinal axis substantially perpendicular to a primary direction of flow of said gas fluid through said gas inlet, a set of nozzles adapted to spray a liquid into said energy and particle recuperator, liquid sprayed via said set of nozzles adapted to collect particulates entrained in said gas fluid, said liquid sprayed via said set of nozzles adapted to receive heat energy from said gas fluid, said energy and particle recuperator defining a heat exchange fluid channel with serrated surfaces, said heat exchange fluid channel substantially surrounding at least a portion of said substantially cylindrical portion of said energy and particle recuperator, said heat exchange fluid channel adapted to receive a heat transfer fluid, said energy and particle recuperator adapted to cause heat energy to be transferred from said gas fluid to said heat transfer fluid without said heat transfer fluid directly contacting said gas fluid.   
   
   
       2 . The system of  claim 1 , further comprising:
 said set of nozzles.   
   
   
       3 . The system of  claim 1 , further comprising:
 a heat exchanger adapted to receive said liquid sprayed via said set of nozzles, said heat exchanger adapted to transfer heat energy from said liquid sprayed via said set of nozzles to a clean process fluid.   
   
   
       4 . The system of  claim 1 , further comprising:
 a heat exchanger adapted to transfer heat energy from said liquid sprayed via said set of nozzles to a clean process fluid, said heat exchanger comprising a set of pipes, each of said set of pipes defining a longitudinal axis, each of said set of longitudinal axes substantially parallel, each of said set of pipes comprising a substantially planar surface over at least a portion of a pipe length so as to partially define a channel between each pair of adjacent pipes of said set of pipes, a cross-section of each pipe at said portion of said pipe length comprising a pair of substantially parallel opposing planar sides with at least one rounded edge, each of said set of pipes comprising ends having a substantially circular cross-section, each of said set of pipes comprising fins.   
   
   
       5 . The system of  claim 1 , further comprising:
 a heat exchanger adapted to transfer heat energy from said liquid sprayed via said set of nozzles to a clean process fluid, said heat exchanger comprising a set of pipes, each of said set of pipes defining a longitudinal axis, each of said set of longitudinal axes substantially parallel, each of said set of pipes comprising a substantially planar surface over at least a portion of a pipe length so as to partially define a channel between each pair of adjacent pipes of said set of pipes, a cross-section of each pipe at said portion of said pipe length comprising a pair of substantially parallel opposing planar sides with at least one rounded edge, each of said set of pipes comprising ends having a substantially circular cross-section, each of said set of pipes comprising dimples.   
   
   
       6 . The system of  claim 1 , further comprising:
 a heat exchanger adapted to transfer heat energy from said liquid sprayed via said set of nozzles to a clean process fluid, said heat exchanger comprising a set of pipes, each of said set of pipes defining a longitudinal axis, each of said set of longitudinal axes substantially parallel, each of said set of pipes comprising a substantially planar surface over at least a portion of a pipe length so as to partially define a channel between each pair of adjacent pipes of said set of pipes, each channel interrupted by connection areas between pairs of adjacent pipes, a cross-section of each pipe at said portion of said pipe length comprising a pair of substantially parallel opposing planar sides with at least one rounded edge, each of said set of pipes comprising ends having a substantially circular cross-section, each of said set of pipes comprising dimples.   
   
   
       7 . The system of  claim 1 , further comprising:
 a heat exchanger adapted to transfer heat energy from said liquid sprayed via said set of nozzles to a clean process fluid, said heat exchanger comprising a set of pipes, each of said set of pipes defining a longitudinal axis, each of said set of longitudinal axes substantially parallel, each of said set of pipes comprising a substantially planar surface over at least a portion of a pipe length so as to partially define a channel between each pair of adjacent pipes of said set of pipes, each channel interrupted by connection areas between pairs of adjacent pipes, each connection area defining a substantially rhombic shape, a cross-section of each pipe at said portion of said pipe length comprising a pair of substantially parallel opposing planar sides with at least one rounded edge, each of said set of pipes comprising ends having a substantially circular cross-section, each of said set of pipes comprising dimples.   
   
   
       8 . The system of  claim 1 , further comprising:
 a heat exchanger adapted to transfer heat energy from said liquid sprayed via said set of nozzles to a clean process fluid, said heat exchanger comprising a set of pipes, each of said set of pipes defining a longitudinal axis, each of said set of longitudinal axes substantially parallel, each of said set of pipes comprising a substantially planar surface over at least a portion of a pipe length so as to partially define a serpentine channel between each pair of adjacent pipes of said set of pipes, a cross-section of each pipe at said portion of said pipe length comprising a pair of substantially parallel opposing planar sides with at least one rounded end, each of said set of pipes comprising ends having a substantially circular cross-section, each of said set of pipes comprising dimples.   
   
   
       9 . The system of  claim 1 , further comprising:
 a particle separator adapted to remove said particulates from said liquid sprayed via said set of nozzles.   
   
   
       10 . The system of  claim 1 , further comprising:
 a pump adapted to cause said liquid sprayed via said set of nozzles to be conveyed to said set of nozzles.   
   
   
       11 . The system of  claim 1 , further comprising:
 a fan adapted to cause said gas fluid to be conveyed through said energy and particle recuperator.   
   
   
       12 . The system of  claim 1 , wherein:
 a set of spacers adapted to maintain a dimension of said channel.   
   
   
       13 . The system of  claim 1 , wherein:
 said central longitudinal axis is substantially horizontal.   
   
   
       14 . The system of  claim 1 , wherein:
 said heat transfer fluid flows substantially counter-current to a flow of said gas fluid.   
   
   
       15 . A method comprising a plurality of activities, comprising:
 causing a gas fluid to be channeled through a substantially horizontal vessel, wherein said substantially horizontal vessel defines an inner shell and an outer shell, a heat exchange fluid channel defined by said inner shell and said outer shell, said heat exchange fluid channel comprising serrated heat transfer surfaces, said heat exchange fluid channel adapted to receive a heat transfer fluid flow, said heat transfer fluid flow adapted to remove heat energy from said gas fluid, said heat transfer fluid flow adapted to convey said heat energy to an energy user, a set of nozzles adapted to spray a liquid into said vessel, liquid sprayed via said set of nozzles adapted to collect particulates entrained in said gas fluid, said liquid sprayed via said set of nozzles adapted to receive heat energy from said gas fluid.   
   
   
       16 . The method of  claim 15 , further comprising:
 removing said particulates from said sprayed liquid via a particle separator.   
   
   
       17 . The method of  claim 15 , further comprising:
 via a heat exchanger, transferring heat energy from said sprayed liquid to a clean process fluid.   
   
   
       18 . A method comprising a plurality of activities, comprising:
 channeling a gas fluid through a substantially horizontal vessel, wherein said substantially horizontal vessel defines an inner shell and an outer shell, a heat exchange fluid channel defined by said inner shell and said outer shell comprising serrated heat transfer surfaces, said heat exchange fluid channel adapted to receive a heat transfer fluid flow, said heat transfer fluid flow adapted to remove heat energy from said gas fluid, said heat transfer fluid flow adapted to convey said heat energy to an energy user, a set of nozzles adapted to spray a liquid into said vessel, liquid sprayed via said set of nozzles adapted to collect particulates entrained in said gas fluid, said liquid sprayed via said set of nozzles adapted to receive heat energy from said gas fluid.

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