Advanced flash exhaust heat recovery

• US 10,267,511 B2
• Filed: 10/12/2017
• Issued: 04/23/2019
• Est. Priority Date: 07/15/2016
• Status: Active Grant

• Current Assignee: BioLeap, Inc.
• Original Assignee: BioLeap, Inc.
• Inventors: Knight, Jr., James, Mitchell, Olan Wayne
• Primary Examiner(s): Yuen, Jessica
• Application Number:
  US15/782,220
• Publication Number:
  US 20180031227A1
• Time in Patent Office: 558 Days
• CPC Class Codes: B01D 47/00 Separating dispersed particles from gases, air or vapours by liquid as separating agent B01D45/10 takes precedence; fractionating columns or parts thereof B01D3/16
• CPC Class Codes: B01D 53/265 by refrigeration (condensation)
• CPC Class Codes: F22B 1/14 coming in direct contact with water in bulk or in sprays
• CPC Class Codes: F22B 1/16 the heat carrier being hot liquid or hot vapour, e.g. waste liquid, waste vapour
• CPC Class Codes: F22B 3/00 Other methods of steam generation; Steam boilers not provided for in other groups of this subclass
• CPC Class Codes: F26B 2200/02 Biomass, e.g. waste vegetative matter, straw
• CPC Class Codes: F26B 23/02 using combustion heating F26B3/305, F26B13/186, F26B21/001, F26B23/10 take precedence
• CPC Class Codes: Y02B 30/52 Heat recovery pumps, i.e. heat pump based systems or units able to transfer the thermal energy from one area of the premises or part of the facilities to a different one, improving the overall efficiency
• CPC Class Codes: Y02P 70/10 Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working

Abstract

Waste heat is extracted in two stages from the exhaust (20) of a biomass dryer (14) in a grain alcohol plant (10). A boiler circuit (56) provides high pressure steam to a balance of the plant (54). A first energy recovery circuit (36) extracts heat from the exhaust via a non-contact heat exchanger (24) and provides a first relatively lower pressure steam (78) to the balance of the plant, thereby bypassing a portion of the boiler circuit. Working fluids in the boiler and first energy recovery circuits are maintained within boiler water quality specifications and are intermixed to allow the production of the first relatively lower pressure steam without a pressure reduction device. A second energy recovery circuit (44) extracts heat from the exhaust downstream of the first energy recovery circuit using a direct contact heat exchanger (38) and provides a non-boiler quality heated fluid (52) to the balance of the plant.

Claims

1. A system for a plant, the plant comprising a dryer operable to remove moisture from a wet cake and to produce an exhaust gas comprising water vapor, the plant also comprising a balance of plant, the system comprising:

a boiler circuit operable to provide a first steam to the balance of the plant;

a first energy recovery circuit comprising a non-contact heat exchanger operable to extract heat from the exhaust gas and to provide a second steam, having a pressure lower than a pressure of the first steam, to the balance of plant;

a component wherein a portion of the first steam from the boiler circuit is intermixed with a flash vapor produced in the first energy recovery circuit, or a component wherein a liquid from the boiler circuit is intermixed with a liquid from the first energy recovery circuit; and

a second energy recovery circuit comprising a direct contact heat exchanger disposed downstream of the non-contact heat exchanger in a flow path of the exhaust gas, the second energy recovery circuit operable to provide a heated fluid to the balance of plant.

2. The system of claim 1, wherein the first energy recovery circuit further comprises:

a flash vessel comprising a working liquid inlet, a working liquid outlet and a flash vapor outlet;

a working liquid loop interconnecting a working liquid outlet of the non-contact heat exchanger with the flash vessel working liquid inlet, and interconnecting the flash vessel working liquid outlet with a working liquid inlet of the non-contact heat exchanger; and

a thermocompressor comprising a suction side for receiving the flash vapor from the flash vapor outlet of the flash vessel and a motive side for receiving a portion of the first steam from the boiler circuit, the thermocompressor operable to produce the second steam.

3. The system of claim 2, wherein fluids in the boiler circuit and the first energy recovery circuit are intermixed by a makeup fluid flow path to the flash vessel sourced from the boiler circuit.

4. The system of claim 2, wherein fluids in the boiler circuit and the first energy recovery circuit are intermixed by a blowdown flow path from the flash vessel to a boiler feed vessel of the boiler circuit.

5. The system of claim 1, further comprising a wet scrubber disposed between the dryer and the non-contact heat exchanger for saturating the exhaust gas with water vapor.

6. The system of claim 5, further comprising a conduit for delivering condensate from the non-contact heat exchanger to the wet scrubber.

7. The system of claim 1, further comprising a pressure increasing device disposed in the flow path of the exhaust gas upstream of the non-contact heat exchanger, and a pressure control device disposed in the flow path of the exhaust gas downstream of the non-contact heat exchanger, the pressure increasing device and pressure control device cooperatively operable to control a pressure of the exhaust gas in the non-contact heat exchanger.

8. The system of claim 1, wherein the second energy recovery circuit further comprises:

a condensate flash vessel comprising a heated condensate inlet, a cooled condensate outlet and a flash vapor outlet;

a condensate loop interconnecting a heated condensate outlet of the direct contact heat exchanger with the condensate flash vessel heated condensate inlet, and interconnecting the condensate flash vessel cooled condensate outlet with a cooled condensate inlet of the direct contact heat exchanger; and

a thermocompressor comprising a suction side for receiving a flash vapor from the flash vapor outlet of the condensate flash vessel and a motive side for receiving a portion of the first steam from the boiler circuit, the thermocompressor operable to produce the heated fluid as a third steam.

9. The system of claim 1, wherein the second energy recovery circuit further comprises:

a preheater comprising a process water inlet for receiving process water from the balance of the plant and a process water outlet for delivering heated process water to the balance of the plant; and

a condensate loop interconnecting a heated condensate outlet of the direct contact heat exchanger with a heated condensate inlet of the preheater, and interconnecting a cooled condensate outlet of the preheater with a cooled condensate inlet of the direct contact heat exchanger.

10. The system of claim 1, wherein:

the first energy recovery circuit further comprises a first thermocompressor receiving a first portion of the first steam from the boiler circuit on its motive side and receiving the flash vapor on its suction side and operable to produce the second steam as boiler quality steam at its discharge side; and

the second energy recovery circuit further comprises a second thermocompressor receiving a second portion of the first steam from the boiler circuit on its motive side and receiving a condensate flash vapor on its suction side and operable to produce the heated fluid as non-boiler quality steam at its discharge side.

11. A corn ethanol plant comprising the system of claim 1.