Asphalt recovery system and process
An asphalt recovery system may include an extractor, a desolventizer, and an evaporator. During operation, the extractor may receive a solvent and roofing waste and extract asphalt from the roofing waste with the solvent. The desolventizer may receive a solvent-wet solids stream from the extractor and vaporize solvent from the solvent-wet solids stream to yield desolventized solids. The evaporator may receive an asphalt-rich solvent stream from the extractor and vaporize solvent from the stream to produce a solvent stream and an asphalt stream. By configuring the evaporator to operate at a pressure above atmospheric pressure, the boiling point in the evaporator may increase as compared to operating the evaporator at a pressure below atmospheric pressure. In turn, this may keep the viscosity of asphalt within the evaporator less than 500 centipoise, which may improve heat transfer to the asphalt and prevent that asphalt from plugging the evaporator.
1. An asphalt recovery process comprising:
extracting asphalt from roofing waste with a solvent in an extractor to form an asphalt-rich solvent stream and solvent-wet solids stream;
processing the solvent-wet solids in a desolventizer at a pressure below atmospheric pressure to vaporize solvent from the solvent-wet solids stream and yield desolventized solids; and
vaporizing solvent from the asphalt-rich solvent stream in an evaporator, wherein the evaporator is operated at a pressure above atmospheric pressure so as to increase a boiling point of the solvent as compared to operating at a pressure below atmospheric pressure and so that a viscosity of asphalt within the evaporator is less than 500 centipoise.
2. The process of claim 1 , wherein vaporizing solvent from the asphalt-rich solvent stream in the evaporator comprises operating the evaporator at a temperature greater than 250 degrees Fahrenheit.
3. The process of claim 1 , wherein the pressure above atmospheric pressure is a pressure of at least 10 inches of H 2 O, as measured at a liquid outlet of the evaporator, and the viscosity of asphalt within the evaporator is less than 200 centipoise.
4. The process of claim 3 , wherein the pressure above atmospheric pressure is a pressure, as measured at a liquid outlet of the evaporator, ranging from approximately 14 inches of H 2 O to a pressure of approximately 150 inches of H 2 O.
5. The process of claim 1 , wherein solvent comprises at least one of toluene and hexane.
6. The process of claim 5 , wherein vaporizing solvent from the asphalt-rich solvent stream in the evaporator comprises operating the evaporator at a temperature greater than or equal to a boiling point of the solvent.
7. The process of claim 1 , wherein extracting asphalt from roofing waste with the solvent in the extractor comprises operating the extractor at a pressure above atmospheric pressure so as to prevent formation of an explosive atmosphere within the extractor.
8. The process of claim 7 , wherein the extracting asphalt from roofing waste with the solvent in the extractor comprises operating the extractor at a temperature greater than or equal to a boiling point of the solvent so as to create the pressure above atmospheric pressure in the extractor.
9. The process of claim 1 , wherein the evaporator comprises at least one of a rising film evaporator and a falling film evaporator.