초록 ▼

A system and associated method of processing solid waste via a waste gasification process results in usable by-products. The method utilizes a rotary kiln heated to a temperature of at least 800° F. and a reduction chamber, heated to a temperature of at least 1800° F. The solid waste is slowly rotat

A system and associated method of processing solid waste via a waste gasification process results in usable by-products. The method utilizes a rotary kiln heated to a temperature of at least 800° F. and a reduction chamber, heated to a temperature of at least 1800° F. The solid waste is slowly rotated in the kiln for six to eight hours. The solid material is passed through screens to separate the ash from other items. Gases are monitored and transported to the reduction chamber to generate power. The gases are then transported to at least one air pollution control unit to remove contaminants before being vented into the atmosphere.

대표청구항 ▼

1. A method of processing solid waste comprising:heating a rotary kiln; feeding the solid waste into the rotary kiln; rotating the rotary kiln, thereby generating gases and residual solids; removing the residual solids from the rotary kiln; transporting the gases from the rotary kiln to a reduction

1. A method of processing solid waste comprising:heating a rotary kiln; feeding the solid waste into the rotary kiln; rotating the rotary kiln, thereby generating gases and residual solids; removing the residual solids from the rotary kiln; transporting the gases from the rotary kiln to a reduction chamber; heating the gases in the reduction chamber; cooling the gases exiting the reduction chamber; transporting the gases to a spray dryer absorber; treating the gases in the spray dryer absorber to remove contaminants by introducing lime and carbon water mist in the spray dryer absorber; transporting the gases from the spray dryer absorber to a baghouse; and removing further contaminants from the gases in the baghouse. 2. The method of claim 1 wherein the step of heating the rotary kiln comprises heating the rotary kiln to at least 800 degrees Fahrenheit.3. The method of claim 1 wherein the step of heating the gases in the reduction chamber comprises heating the reduction chamber to at least 1,800 degrees Fahrenheit.4. The method of claim 1 further comprising separating the residual solids into components by passing the residual solids through at least one screen to separate ash from other components.5. The method of claim 1 wherein the rotary kiln rotates at approximately one revolution per minute.6. The method of claim 1 wherein the solid waste is rotated in the rotary kiln for six to eight hours.7. The method of claim 1 wherein the reduction chamber is maintained at between approximately 1800-2400 degrees Fahrenheit.8. The method of claim 1 further comprising maintaining the rotary kiln at approximately 800 degrees Fahrenheit.9. The method of claim 1 wherein the gases are heated in the reduction chamber for at least one second.10. The method of claim 1 further comprising collecting particulate from the spray dryer absorber and the baghouse and transporting the particulate to an ashbin.11. The method of claim 1 wherein the gases exiting the spray dryer absorber are at a temperature of approximately 290 degrees Fahrenheit.12. The method of claim 1 further comprising maintaining the gases exiting the rotary kiln at approximately 800 degrees Fahrenheit.13. The method of claim 1 further comprising maintaining the gases entering the spray dryer absorber at a temperature of approximately 500 degrees Fahrenheit.14. The method of claim 1 wherein the step of cooling the gases exiting the reduction chamber comprises spraying water into the gases.15. The method of claim 1 wherein the step of removing further contaminants from the gases in the baghouse comprises passing the gases through filters.16. A method of processing solid waste, said method comprising:feeding the solid waste into an interior of a rotary kiln at a predetermined feed rate; rotating the rotary kiln at a predetermined rotation speed; introducing air into the interior of the rotary kiln; heating the solid waste in the interior of the rotary kiln, thereby generating gases and residual solids; ducting the gases generated in the rotary kiln to a reduction chamber; adjusting at least one of the feed rate of the solid waste into the interior of the rotary kiln, rotation speed of the rotary kiln, and airflow into the interior of the rotary kiln to maintain the temperature of the gases exiting the rotary kiln at between 800-1200 degrees Fahrenheit; ducting the gases from the reduction chamber to a spray dryer absorber; introducing lime and carbon water mist into the spray dryer absorber; and transporting the gases from the spray dryer absorber to a baghouse. 17. The method of claim 16 further comprising collecting the residual solids and separating them into components.18. The method of claim 17 wherein separating the residual solids into components comprises passing the residual solids through at least one screen.19. The method of claim 16 wherein the rotary kiln rotates at approximately one revolution per minute.20. The method of claim 16 wherein the solid waste is rotated in the rotary kiln rotates for six to eight hours.21. The method of claim 16 further comprising heating the reduction chamber to approximately 1800-2400 degrees Fahrenheit.22. The method of claim 16 further comprising collecting particulate from the spray dryer absorber and from the baghouse.23. The method of claim 22 further comprising passing said gases through filters in said baghouse.24. The method of claim 16 wherein the gases exiting the spray dryer absorber are at a temperature of approximately 290 degrees Fahrenheit.25. A system for processing solid waste, said system comprising:a rotary kiln having drive means for rotating the rotary kiln; a feeder for feeding said solid waste into said rotary kiln; a heating system for heating the rotary kiln; a reduction chamber adapted to receive and burn gases generated in the rotary kiln; a heating system for heating the reduction chamber; a spray dryer absorber located downstream of the reduction chamber; a sprayer located at the top of the spray dryer absorber for spraying a lime slurry into said spray dryer absorber to remove contaminants from said gases; and a hopper adapted to receive residual solids generated in the rotary kiln. 26. The system of claim 25 further comprising a baghouse.27. The system of claim 25 further comprising a combustion control system including a plurality of temperature probes for monitoring the temperature of said gases.28. The system of claim 25 further comprising at least one misting nozzle to cool the gases exiting the reduction chamber.