Liquid Evaporation System with Heated Liquid

Abstract

A liquid evaporation system for evaporating clean water from a reservoir of wastewater includes a liquid evaporator to evaporate and separate water vapor from the wastewater in a confined space, an air blower to supply air to the liquid evaporator, and a wastewater heating system arranged to collect heat to heat the wastewater in the reservoir.

We claim: 
     
         1 . A liquid evaporation system for evaporating clean water from a volume of wastewater, the liquid evaporation system comprising:
 a liquid evaporator having a direct contact adiabatic evaporation system operatively arranged to evaporate and separate water vapor from the volume of wastewater within a confined space;   an air blower operatively connected to the liquid evaporator and to supply air to the liquid evaporator for forming the water vapor; and   and a heating system arranged to heat the wastewater.   
     
     
         2 . The liquid evaporation system of  claim 1 , wherein the heating system comprises a waste heat source from an industrial process. 
     
     
         3 . The liquid evaporation system of  claim 2 , wherein the industrial process comprises an electrical power generation plant. 
     
     
         4 . The liquid evaporation system of  claim 2 , wherein the waste heat source comprises low pressure steam turbine exhaust. 
     
     
         5 . The liquid evaporation system of  claim 2 , wherein the waste heat source comprises combustion exhaust gases. 
     
     
         6 . The liquid evaporation system of  claim 5 , wherein the combustion exhaust gases are captured from a boiler, and the heating system includes a heat exchanger arranged to capture exhaust heat from the exhaust gases. 
     
     
         7 . The liquid evaporation system of  claim 1 , wherein the heating system further comprises:
 a heat exchanger hydraulically connected with the volume of wastewater;   a pump arranged to circulate the wastewater from the volume of wastewater to the heat exchanger; and   a waste heat source operatively connected with the heat exchanger;   wherein the heat exchanger is arranged to heat the wastewater with heat from the waste heat source, and the pump is arranged to circulate the heated wastewater from the heat exchanger to the volume of wastewater.   
     
     
         8 . The liquid evaporation system of  claim 7 , further comprising a thermal holding tank operatively connected to the heating system, wherein heated wastewater from the heat exchanger is stored in the thermal holding tank. 
     
     
         9 . The liquid evaporation system of  claim 8 , wherein wastewater is supplied to the liquid evaporator from a holding reservoir, wherein the holding reservoir is operatively connected to the heating system to supply wastewater to the heating system. 
     
     
         10 . The liquid evaporation system of  claim 7 , wherein the waste heat source is operatively connected directly to the heat exchanger. 
     
     
         11 . The liquid evaporation system of  claim 7 , wherein the waste heat source is operatively connected to the heat exchanger with a heat transfer circulation loop. 
     
     
         12 . The liquid evaporation system of  claim 7 , wherein the waste heat source is operatively connected to the heat exchanger with a vapor compression loop. 
     
     
         13 . The liquid evaporation system of  claim 1 , wherein the volume of wastewater is contained in an enclosed vessel defining the confined space, and the liquid evaporator includes a draft tube assembly including a downcomer and a weir disposed in the enclosed vessel and arranged to vigorously mix a volume of air with the volume of wastewater. 
     
     
         14 . The liquid evaporation system of  claim 1 , wherein the volume of wastewater is contained in an open reservoir of wastewater, and the liquid evaporator is disposed in the volume of wastewater. 
     
     
         15 . The liquid evaporation system of  claim 14 , wherein the liquid evaporator comprises:
 a partially enclosed vessel defining the confined space;   an air dispersion chamber inside the confined space for mixing the air with the wastewater;   a downcomer operatively connecting the air blower with the air dispersion chamber;   an exhaust port hydraulically arranged to allow water vapor to exhaust from the vessel; and   a tortuous pathway operatively connecting the air dispersion chamber with the exhaust port.   
     
     
         16 . The liquid evaporation system of  claim 14 , wherein in an operative position, the vessel is disposed at the top surface of the wastewater having a top portion disposed above the top surface and a bottom portion disposed in the wastewater. 
     
     
         17 . The liquid evaporation system of  claim 16 , wherein the liquid evaporator includes a flotation device operatively secured to the vessel, wherein the floatation device maintains the vessel in the operative position by floating on the top surface of the wastewater. 
     
     
         18 . The liquid evaporation system of  claim 16 , wherein the liquid evaporator is maintained in a fixed position in the operative position by braces or legs. 
     
     
         19 . The liquid evaporation system of  claim 1 , further comprising at least a second liquid evaporator operatively disposed in the wastewater. 
     
     
         20 . The liquid evaporation system of  claim 13 , wherein the liquid evaporator comprises a demister arranged to separate entrained wastewater from the water vapor. 
     
     
         21 . A method of evaporating water vapor from a volume of wastewater, the method comprising the steps of:
 evaporating the water vapor with a liquid evaporator including a direct contact adiabatic evaporation system; and   heating the wastewater with waste heat from an industrial process.   
     
     
         22 . The method of  claim 21 , wherein the step of heating includes the steps of:
 collecting exhaust heat energy from the industrial process; and   transferring the collected exhaust heat energy to the volume of wastewater.   
     
     
         23 . The method of  claim 22 , wherein the industrial process comprises an electric power generation plant. 
     
     
         24 . The method of  claim 21 , wherein the liquid evaporator comprises a downcomer and an air dispersion chamber, wherein the downcomer includes an air discharge outlet disposed inside the air dispersion chamber and arranged to vigorously mix gases with the wastewater inside the air dispersion chamber. 
     
     
         25 . The method of  claim 24 , wherein the volume of wastewater is contained in an open reservoir, the liquid evaporator comprises a partially enclosed vessel disposed in the reservoir, the air dispersion chamber disposed inside the partially enclosed vessel, and an exhaust port from the partially enclosed vessel in fluid communication with the air dispersion chamber, the method further comprising the steps of:
 disposing the partially enclosed vessel at a top surface of the wastewater;   drawing air into the wastewater inside the air dispersion chamber;   exhausting water vapor from the air dispersion chamber out through the exhaust port.   
     
     
         26 . The method of  claim 24 , wherein the volume of wastewater is contained in an enclosed tank.