Heat recovery from a biomass heat source

• US 7,566,383 B2
• Filed: 06/17/2005
• Issued: 07/28/2009
• Est. Priority Date: 06/17/2005
• Status: Active Grant

• Current Assignee: Aventine Renewable Energy Holdings, Purdue Research Foundation (The Trustees of Purdue University (d/b/a Purdue University))
• Original Assignee: Purdue Research Foundation (The Trustees of Purdue University (d/b/a Purdue University))
• Inventors: Everett, Rollo J., Weiland, Jerry L., Welch, Gary, Mosier, Nathan S., Ladisch, Michael R.
• Primary Examiner(s): Manoharan; Virginia
• Application Number:
  US11/156,242
• Publication Number:
  US 20060286628A1
• Time in Patent Office: 1,502 Days
• Field of Search: 621/71, 621/83, 623/04, 95/17, 952/88, 159/2.1, 159/2.3, 159/47.3, 159/901, 159/DIG.8, 159/DIG.22, 159/DIG.23, 202/185.2, 203/88, 203/DIG.8, 210/774, 435/161, 435/162, 426/476
• US Class Current: 203/88
• CPC Class Codes: B01D 3/06 Flash distillation
• CPC Class Codes: B01D 5/0027 by direct contact between vapours or gases and the cooling medium
• CPC Class Codes: B01D 5/006 with evaporation or distillation
• CPC Class Codes: F28B 3/00 Condensers in which the steam or vapour comes into direct contact with the cooling medium
• CPC Class Codes: Y02E 50/10 Biofuels, e.g. bio-diesel
• 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
• CPC Class Codes: Y10S 159/08 Multieffect or multistage
• CPC Class Codes: Y10S 159/22 Condensate flashing
• CPC Class Codes: Y10S 159/23 Cooling
• CPC Class Codes: Y10S 203/08 Waste heat

Abstract

A method and system for recovering heat from a pretreated hot biomass stream is described. The method and system for heat recovery includes a flash cooler connected to a direct contact condenser. A liquid portion of the hot biomass stream flashes into vapors upon the hot biomass stream entering the flash cooler. The flashed vapors are transferred to the direct contact condenser. The flashed vapors and an incoming cold biomass stream subsequently come into contact with each other in the direct contact condenser, thereby causing heat to be transferred from the hot biomass stream to the cold biomass stream. As the heat transfer occurs, the flashed vapors condense onto the surface of the cold biomass.

Claims

1. A method for transferring heat from a first hot biomass to a cold biomass, comprising the steps of:

(a) providing a heat recovery system, comprising;

a flash cooler; and

a direct contact condenser;

(b) providing a first hot biomass stream characterized by a first temperature and a first pressure, and having a liquid with a first saturation water vapor pressure at the first temperature;

(c) introducing the first hot biomass stream into the flash cooler, the flash cooler having a second pressure, where the second pressure is less than the first saturation water vapor pressure and the second pressure is less than the first pressure;

(d) flashing a liquid portion of the first hot biomass to form a first hot biomass vapor and an unflashed first hot biomass component, the first hot biomass vapor having a second temperature that is less than the first temperature;

(e) removing the first hot biomass vapor from the flash cooler;

(f) transferring the first hot biomass vapor into the direct contact condenser;

(g) introducing a cold biomass into the direct contact condenser, the cold biomass having a third temperature, where the third temperature is less than the second temperature of the first hot biomass vapor; and

(h) contacting the first hot biomass vapor with the cold biomass for a time sufficient to transfer heat from the first hot biomass vapor to the cold biomass, wherein the first hot biomass vapor condenses onto the cold biomass, wherein the transfer of heat to the cold biomass increases the temperature of the cold biomass to form a heated cold biomass having a fourth temperature, where the fourth temperature is greater than the third temperature.

2. The method of claim 1, wherein contacting the first hot biomass vapor with the cold biomass comprises countercurrent flow of the vapor and the cold biomass into the direct contact condenser.

3. The method of claim 1 further comprising the steps of:

(i) withdrawing the heated cold biomass from the direct contact condenser,

(j) increasing the temperature of the heated cold biomass to the first temperature of the first hot biomass stream; and

(k) pretreating the heated cold biomass at the first temperature to form a second hot biomass stream.

4. The method of claim 3 wherein the first temperature is about 320°

F.

5. The method of claim 3 wherein the temperature of the heated cold biomass is increased to the first temperature of the first hot biomass comprises direct steam injection heating of the heated cold biomass.

6. The method of claim 1 wherein the first hot biomass stream comprises a pretreated cellulosic liquid slurry.

7. The method of claim 6 wherein the first pressure is between about 70 to 90 psig.

8. The method of claim 6 wherein the third temperature is about 212°

F.

9. The method of claim 6 wherein the fourth temperature is about 264°

F.

10. The method of claim 1 wherein the first hot biomass stream is selected from the group consisting of corn fiber and corn stover.

11. The method of claim 10 wherein the first temperature is about 320°

F.

12. The method of claim 1 wherein the second temperature of the first hot biomass vapor is about 264°

F.

14. The method of claim 1 where the first pressure of the first hot biomass stream is at least about 1% greater than the first saturation water vapor pressure.

15. The method of claim 1, where the flash cooler is a first flash cooler and the direct contact condenser is a first direct contact condenser, and where the method further comprising the steps of:

(a) providing a second flash cooler positioned to receive the unflashed first hot biomass component from the first flash cooler; and

a second direct contact condenser positioned to receive a second hot biomass vapor from the second flash cooler;

(b) introducing the unflashed first hot biomass component into the second flash cooler, the unflashed first hot biomass component having the second temperature, the second flash cooler having a pressure less than second the pressure of the first flash cooler;

(c) flashing a liquid portion of the unflashed first hot biomass component to form the second hot biomass vapor and an unflashed second hot biomass component, where the second hot biomass vapor has a fifth temperature, where the fifth temperature is less than the second temperature;

(d) transferring the second hot biomass vapor into the second direct contact condenser;

(e) introducing a second cold biomass having a sixth temperature, where the sixth temperature is lower than the fifth temperature of the second hot biomass vapor;

(f) contacting the second cold biomass with the second hot biomass vapor in the second direct contact condenser for a time sufficient to transfer heat from the second hot biomass vapor to the second cold biomass, wherein the second hot biomass vapor condenses onto the surface of the second cold biomass, wherein the transfer of heat to the second cold biomass increases the temperature of the second cold biomass.

16. The method of claim 15 further comprising the step of

(g) providing a stand alone direct contact condenser and transferring a remaining uncondensed second hot biomass vapor from the second direct contact condenser to the stand alone direct contact condenser, where the remaining uncondensed second hot biomass vapor has a seventh temperature, where the seventh temperature is less than the fifth temperature of the second hot biomass vapor;

(h) introducing a third cold biomass material into the stand alone direct contact condenser having a temperature less than the seventh temperature of the remaining uncondensed second hot biomass vapor; and

(i) contacting the third cold biomass material with the remaining uncondensed second hot biomass vapor in the stand alone direct contact condenser for a time sufficient to transfer heat from the remaining uncondensed second hot biomass vapor to the third cold biomass material, wherein absorption of the heat by the material condenses the remaining uncondensed second hot biomass vapor onto the surface of the material.

17. The method of claim 16 where the third cold biomass material comprises stillage.

18. The method of claim 15 further comprising the steps of:

(g) removing the unflashed second hot biomass component from the second flash cooler;

(h) providing a centrifuge and introducing the unflashed second hot biomass component into the centrifuge, where the centrifuge separates the unflashed second hot biomass component into a solid cake and a liquid product.

13. The method of clam 1 comprising recycling the unflashed first hot biomass component comprising the steps of:

(i) withdrawing the unflashed first hot biomass component from the flash cooler, where the unflashed first hot biomass component has a temperature that is less than the first temperature;

(j) increasing the temperature of the unflashed first hot biomass component to the first temperature of the first hot biomass stream; and

(k) pretreating the unflashed first hot biomass component heated to the first temperature to form a third hot biomass stream.

19. A method for controlled and incremental transfer of heat from a hot biomass to a cold biomass, comprising the steps of:

(a) providing a heat recovery system comprising a plurality of flash coolers configured in series to permit the flow of an unflashed hot biomass component from a first flash cooler to one or more downstream flash coolers and a plurality of direct contact condensers configured in series to permit the flow of a flashed hot biomass from a first direct contact condenser to one or more downstream direct contact condensers, wherein each of the plurality of flash coolers is operably connected to a corresponding direct contact condenser;

(b) generating an unflashed hot biomass component in the first flash cooler and subsequently sequentially passing the hot biomass through the plurality of flash coolers;

(c) heating a cold biomass and sequentially passing the cold biomass through the plurality of direct contact condensers;

(d) flashing a liquid portion of the hot biomass into a vapor within each of the plurality of flash coolers that the hot biomass passes through;

(e) removing the vapor from each of the plurality of flash coolers;

(f) transferring the vapor from each of the plurality of flash coolers to the corresponding direct contact condenser;

(g) contacting the vapor with the cold biomass in each of the corresponding direct contact condensers the cold biomass sequentially passes through; and

(h) condensing the vapor onto a surface of the cold biomass, thereby heating the cold biomass sequentially passing through each of the corresponding direct contact condensers.

20. The method of claim 19 for the controlled and incremental transfer of heat from a hot biomass to a cold biomass where undesirable formation of degradation products in the unflashed hot biomass component is minimized.

21. A method for controlled and incremental transfer of heat from a hot biomass stream to a cold biomass stream, comprising the steps of:

(a) providing a heat recovery system, comprising;

a first flash cooler;

a second flash cooler; and

a direct contact condenser;

(b) providing the hot biomass stream characterized by a first temperature and a first pressure, and having a liquid with a first saturation water vapor pressure at the first temperature

(c) introducing the hot biomass stream into the first flash cooler, the first flash cooler having a second pressure, where the second pressure is less than the first saturation water vapor pressure and the second pressure is less than the first pressure;

(d) flashing a portion of the liquid of the first hot biomass stream to form a first hot biomass vapor and an unflashed first hot biomass component, the first hot biomass vapor having a second temperature that is less than the first temperature;

(e) removing the first hot biomass vapor from the first flash cooler;

(f) transferring the unflashed first hot biomass component having the second temperature into the second flash cooler;

(g) flashing a liquid portion of the unflashed first hot biomass component to form a second hot biomass vapor and an unflashed second hot biomass component, the second hot biomass vapor having a third temperature less than the second temperature;

(h) transferring the first hot biomass vapor from the first flash cooler and the second hot biomass vapor from the second flash cooler into the direct contact condenser;

(i) introducing a cold biomass stream into the direct contact condenser, the cold biomass having a fourth temperature, where the fourth temperature is less than the second temperature of the first hot biomass vapor and the third temperature of the second hot biomass vapor; and

(j) contacting the first hot biomass vapor and the second hot biomass vapor with the cold biomass for a time sufficient to transfer heat from the first hot biomass vapor and heat from the second hot biomass vapor to the cold biomass, wherein absorption of the heats from the first and second hot biomass vapors by the cold biomass condenses the first and second hot biomass vapors onto the surface of the cold biomass, wherein the transfer of heat to the cold biomass increases the fourth temperature of the cold biomass to form a heated cold biomass having a fifth temperature, wherein the fifth temperature of the heated cold biomass is greater than the fourth temperature of the cold biomass.

22. The method of claim 21, wherein the controlled and incremental transfer of heat from the hot biomass stream to the cold biomass stream reduces formation of sugar degradation products.