Dryer exhaust heat recovery
Waste heat is extracted from the exhaust ( 20 ) of a biomass dryer ( 14 ) in a grain alcohol plant ( 10 ). A boiler circuit ( 74 ) provides high pressure steam to a balance of the plant ( 64 ). A recovered energy circuit ( 76 ) extracts heat from the exhaust via a dryer exhaust condensing economizer ( 24 ) and provides a steam mixture ( 60 ) to satisfy an intermediate pressure steam demand of the balance of the plant, thereby bypassing a portion of the boiler circuit. Working fluids in the boiler and recovered energy circuits are intermixed in a boiler feed vessel ( 72 ). Dryer exhaust condensate ( 30 ) may be used in an exhaust gas scrubber ( 22 ) upstream of the dryer exhaust condensing economizer to remove pollutants and to saturate ( 26 ) the exhaust gas for improved heat transfer. Heat transfer may be further improved by operating the dryer exhaust condensing economizer at an elevated pressure.
1. A system for a plant, the plant including a dryer operable to remove moisture from a wet cake and to produce dryer exhaust gas comprising water vapor, the plant also including an apparatus operable to produce a plant process vapor, the system comprising:
a dryer exhaust condensing economizer comprising an exhaust gas inlet for receiving the dryer exhaust gas and an exhaust gas outlet for discharging dehydrated dryer exhaust gas, and further comprising a working liquid inlet and a working liquid outlet;
a flash vessel comprising a working liquid inlet, a working liquid outlet and a flash vapor outlet;
a working liquid loop interconnecting the dryer exhaust condensing economizer working liquid outlet with the flash vessel working liquid inlet, and interconnecting the flash vessel working liquid outlet with the dryer exhaust condensing economizer working liquid inlet; and
a thermocompressor comprising a suction side for receiving a flash vapor from the flash vapor outlet of the flash vessel and a motive side for receiving the plant process vapor, the thermocompressor operable to produce a vapor mixture;
wherein during operation of the plant, the improvement is effective to move heat from the dryer exhaust gas into the vapor mixture via the working liquid loop for use in the plant.
2. The system of claim 1 , further comprising a wet scrubber disposed between the dryer and the dryer exhaust condensing economizer for saturating the dryer exhaust gas with water vapor upstream of the dryer exhaust condensing economizer exhaust gas inlet.
3. The system of claim 2 , further comprising a conduit for delivering dryer exhaust condensate from the dryer exhaust condensing economizer to the wet scrubber.
4. The system of claim 1 , further comprising a pressure increasing device disposed in a flow path of the dryer exhaust gas upstream of the dryer exhaust condensing economizer, and a pressure control device disposed in the flow path of the dryer exhaust gas downstream of the dryer exhaust condensing economizer, the pressure increasing device and pressure control device cooperatively operable to control a pressure of the dryer exhaust gas in the dryer exhaust condensing economizer.
5. A corn ethanol plant comprising the system of claim 1 .
6. A plant comprising the system of claim 1 , wherein the plant process vapor and the vapor mixture comprise steam.
7. A system for use in a grain alcohol plant, the grain alcohol plant including a dryer operable to remove moisture from a wet cake and to produce dryer exhaust gas comprising water vapor, the grain alcohol plant also including a boiler operable to produce plant steam, the system comprising:
a dryer exhaust condensing economizer operable to use liquid water as a cooling fluid to condense water vapor from the dryer exhaust gas;
a flash vessel in water loop communication with the dryer exhaust condensing economizer and operable to produce flash water vapor when receiving heated water from the dryer exhaust condensing economizer and returning flash cooled water to the dryer exhaust condensing economizer;
a thermocompressor operable to produce an intermediate pressure steam mixture when receiving the flash water vapor at a relatively lower pressure and the plant steam at a relatively higher pressure, the intermediate pressure steam usable in the grain alcohol plant; and
a boiler loop of the grain alcohol plant in fluid communication with the flash vessel.
8. The system of claim 7 , further comprising a scrubber disposed between the dryer and the dryer exhaust condensing economizer.
9. The system of claim 8 , wherein the scrubber comprises a wet scrubber, and further comprising a conduit for delivering dryer exhaust condensate from the dryer exhaust condensing economizer to the wet scrubber.
10. The system of claim 7 , further comprising a pressure increasing device disposed in a flow path of the dryer exhaust gas upstream of the dryer exhaust condensing economizer and a pressure control device disposed in the flow path of the dryer exhaust gas downstream of the dryer exhaust condensing economizer, the pressure increasing device and pressure control device cooperatively operable to control a pressure of the dryer exhaust gas in the dryer exhaust condensing economizer.
11. A corn ethanol plant comprising the system of claim 7 .
12. A method of recovering heat from dryer exhaust gas comprising water vapor in a plant, the plant comprising a dryer operable to remove moisture from a wet cake and to produce the dryer exhaust gas comprising water vapor, the plant also comprising an apparatus operable to produce a plant process vapor, the method comprising:
directing the dryer exhaust gas and cooled working liquid into a dryer exhaust condensing economizer;
discharging dehydrated dryer exhaust gas and heated working liquid from the dryer exhaust condensing economizer;
directing the heated working liquid into a flash vessel to produce the cooled working liquid and a flash vapor;
directing the flash vapor to a suction side of a thermocompressor and directing the plant process vapor to a motive side of the thermocompressor to produce a vapor mixture;
wherein the method is effective to move heat from the dryer exhaust gas into the vapor mixture via the working liquid for use in the plant.
13. The method of claim 12 , further comprising saturating the dryer exhaust gas with water vapor in a wet scrubber upstream of the dryer exhaust condensing economizer.
14. The method of claim 13 , further comprising delivering dryer exhaust condensate from the dryer exhaust condensing economizer to the wet scrubber.
15. The method of claim 12 , further comprising controlling a pressure of the dryer exhaust gas in the dryer exhaust condensing economizer with a pressure increasing device disposed in a flow path of the dryer exhaust gas upstream of the dryer exhaust condensing economizer and a pressure control device disposed in the flow path of the dryer exhaust gas downstream of the dryer exhaust condensing economizer.
16. A method of recovering heat from a dryer exhaust gas of a corn ethanol plant, the method comprising practicing the method of claim 12 in the corn ethanol plant.
17. A method of recovering heat from a dryer exhaust gas of a plant, the method comprising practicing the method of claim 12 in the plant wherein the plant process vapor and the vapor mixture comprise steam.
18. A method of recovering heat from a dryer exhaust gas comprising water vapor in a grain alcohol plant, the plant comprising a dryer operable to remove moisture from a wet cake and to produce the dryer exhaust gas comprising water vapor, the plant also comprising a boiler loop operable to produce plant steam, the method comprising:
condensing water vapor from the dryer exhaust gas in a dryer exhaust condensing economizer using flash cooled liquid water as a cooling fluid and producing dehydrated dryer exhaust gas and heated liquid water;
directing the heated liquid water to a flash vessel in water loop communication with the dryer exhaust condensing economizer to produce flash water vapor and the flash cooled water;
directing the flash water vapor at a relatively lower pressure and the plant steam at a relatively higher pressure to a thermocompressor to produce an intermediate pressure steam mixture, the intermediate pressure steam mixture usable in the grain alcohol plant; and
placing the boiler loop of the grain alcohol plant in fluid communication with the flash vessel.
19. The method of claim 18 , further comprising disposing a scrubber between the dryer and the dryer exhaust condensing economizer.
20. The method of claim 19 , wherein the scrubber comprises a wet scrubber, and further comprising delivering dryer exhaust condensate from the dryer exhaust condensing economizer to the wet scrubber.
21. The method of claim 18 , further comprising disposing a pressure increasing device in a flow path of the dryer exhaust gas upstream of the dryer exhaust condensing economizer and a pressure control device in the flow path of the dryer exhaust gas downstream of the dryer exhaust condensing economizer, and operating the pressure increasing device and pressure control device to control a pressure of the dryer exhaust gas in the dryer exhaust condensing economizer.
22. A method of recovering heat from a dryer exhaust gas in a corn ethanol plant, the method comprising practicing the method of claim 18 in the corn ethanol plant.