Method to maximize energy recovery in waste-to-energy process

Abstract

In a fossil fuel waste incineration or plasma gasification process, waste heat generated by combustion of waste is captured by a heat transfer fluid and conveyed to an Organic Rankine Cycle (ORC) for energy recovery. In the case of a fossil fuel-fired waste incineration system, the heat transfer fluid captures waste heat from a double-walled combustion chamber, a heat exchanger being used to cool the hot process exhaust (gas cooler). In the case of a plasma waste gasification system, the heat transfer fluid captures waste heat from a plasma torch, a gasification chamber and combustion chamber cooling jackets as well as any other high-temperature components requiring cooling, and then a heat exchanger used to cool the hot process exhaust (gas cooler). The heat exchanger may take on several configurations, including plate or shell and tube configurations.

1 . A fossil fuel waste incineration or plasma gasification process, wherein waste heat generated by a combustion of waste is captured by a heat transfer fluid and conveyed to an Organic Rankine Cycle (ORC) for energy recovery. 
     
     
         2 . The process according to  claim 1 , wherein, in a fossil fuel-fired waste incineration system, the heat transfer fluid captures waste heat from a double-walled combustion chamber, a heat exchanger being used to cool the hot process exhaust. 
     
     
         3 . The process according to  claim 2 , wherein the heat exchanger comprises a plate or a shell and tube configuration. 
     
     
         4 . The process according to  claim 1 , wherein, in a plasma waste gasification system, the heat transfer fluid captures waste heat from at least one of a plasma torch, a gasification chamber cooling jacket and a combustion chamber cooling jacket, and a heat exchanger being then used to cool the hot process exhaust. 
     
     
         5 . The process according to  claim 4 , wherein the heat transfer fluid further captures waste heat from any other high-temperature components requiring cooling. 
     
     
         6 . The process according to  claim 4 , wherein, wherein the heat exchanger comprises a plate or a shell and tube configuration. 
     
     
         7 . The process according to  claim 1 , wherein the hot heat transfer fluid exits the exhaust heat exchanger and is fed to an Organic Rankine Cycle (ORC) evaporator, the thermal energy carried thereby being transferred to the refrigerant for conversion into electricity. 
     
     
         8 . The process according to  claim 1 , wherein the hot heat transfer fluid is fed to a separate, secondary heat exchanger until an appropriate temperature has been reached for proper operation of the ORC or in case of a process and ORC unit malfunction. 
     
     
         9 . The process according to  claim 8 , wherein the temperature of the heat transfer fluid is monitored and the fluid is fed to the ORC evaporator system or to the secondary heat exchanger system based on whether or not the temperature of the fluid falls within an operating temperature of the ORC system, allowing the heat transfer fluid to be fed to the secondary heat exchanger in case of ORC system failure thus allowing the waste destruction system to continue operating without interruption. 
     
     
         10 . A process of operating a waste destruction system at a higher shell temperature to allow for the generation of a useful hot liquid resource, using high temperature polymeric material in plasma torch components and insulation of the hot components of the system. 
     
     
         11 . The process according to  claim 1 , wherein the waste thermal energy in the process is recovered by cooling of the various thermal components with the liquid and by using the liquid to quench the hot process exhaust. 
     
     
         12 . The process according to  claim 11 , wherein energy is recovered from the heated liquid following a filtration step to remove any entrapped ash. 
     
     
         13 . A method, wherein waste thermal energy in a fossil fuel waste incineration or plasma gasification process is recovered by cooling of the various thermal components with a liquid and by using the liquid to quench the hot process exhaust. 
     
     
         14 . The method according to  claim 13 , wherein energy is recovered from the heated liquid following a filtration step to remove any entrapped ash. 
     
     
         15 . A method, wherein the waste thermal energy in a fossil fuel waste incineration or plasma gasification process is recovered by cooling of the various thermal components with a fluid and by using the fluid to indirectly cool the recirculated filtered quench water. 
     
     
         16 . The process according to  claim 1 , wherein the waste thermal energy in the process is recovered by cooling of the various thermal components with a fluid and by using the fluid to indirectly cool the recirculated filtered quench water. 
     
     
         17 . The process according to  claim 1 , wherein the hot liquid, containing the thermal energy recovered from heated parts of the waste destruction system, can be used as a resource for other surrounding processes. 
     
     
         18 . The process according to  claim 1 , wherein the method is used as a way of preheating water for use in a boiler, if the option of steam generation is retained.