IP Library Granted Patent US 8,900,370
Granted Patent B2
US 8,900,370 · App. 12/181,565 · Granted Dec 2, 2014

Method and apparatus for conveying a cellulosic feedstock

Inventors: Quang A. Nguyen (Chesterfield, MO); Sunalie N. Hillier (Georgetown, CA); Murray J. Burke (Oakville, CA)
Assignee: Abengoa Bioenergy New Technologies, LLC.
C13K1/02B01F5/00Y02E50/16C13K13/00B01F3/20
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Quick Facts
Patent No.
US 8,900,370
App. No.
12/181,565
Granted
Dec 2, 2014
Kind
B2
Abstract

A method and apparatus for preparing a cellulosic feedstock are disclosed. Embodiments of the method comprise obtaining a cellulosic feedstock having a moisture content of 30 wt % to 60 wt %; passing the cellulosic feedstock through a heated holding tank; withdrawing the cellulosic feedstock from the holding tank; and, subsequently subjecting the cellulosic feedstock to hydrolysis. Embodiments of the apparatus comprise at least one sidewall defining a volume having an upper portion and a lower portion. At least one inlet is provided adjacent the upper portion, and the inlet is in fluid communication with an impregnation chamber provided upstream from the holding tank. At least one outlet is provided adjacent the lower portion, and the outlet is in fluid communication with hydrolysis reactor positioned downstream from the holding tank. At least one conveyor is positioned adjacent the at least one outlet. A heating jacket provided on at least a portion of the apparatus.

Claims (30)

1. A method for preparing a cellulosic feedstock comprising:

(a) obtaining a cellulosic feedstock having a moisture content of 30 wt % and 60 wt %;

(b) passing the moistened cellulosic feedstock through a heated holding tank, the heated holding tank comprising (i) at least one sidewall defining a passage having an upper portion and a lower portion, (ii) at least one inlet adjacent to the upper portion, and (iii) at least one outlet adjacent the lower portion, wherein the holding tank has a longitudinal axis and at least one of the at least one sidewalls diverges from the longitudinal axis from the upper portion to the lower portion;

(c) withdrawing the cellulosic feedstock from the at least one outlet of the heated holding tank; and,

(d) subsequently subjecting the cellulosic feedstock to hydrolysis.

2. The method of claim 1 , wherein the moisture content of the moistened cellulosic feedstock is between 45 wt % and 55 wt %.

3. The method of claim 1 , wherein step (b) comprises passing the moistened cellulosic feedstock downwardly through the heated holding tank.

4. The method of claim 3 , wherein the moistened cellulosic feedstock is passed downwardly through the heated holding tank under the force of gravity.

5. The method of claim 1 , wherein the moistened cellulosic feedstock has a residence time of up to 60 minutes in the heated holding tank.

6. The method of claim 1 , wherein the moistened cellulosic feedstock has a residence time of between 5 minutes and 45 minutes in the heated holding tank.

7. The method of claim 1 , wherein moistened cellulosic feedstock has a residence time of between 10 minutes and 30 minutes in the heated holding tank.

8. The method of claim 1 , wherein the heated holding tank is heated by passing a heated fluid through a heating jacket provided on at least a portion of the heated holding tank.

9. The method of claim 1 , wherein the moistened cellulosic feedstock enters the heated holding tank at a temperature of between 50° C. and 70° C.

10. The method of claim 1 , wherein the moistened cellulosic feedstock enters the heated holding tank at a temperature between 50° C. and 65° C.

11. The method of claim 1 , further comprising maintaining the moistened cellulosic feedstock at a temperature of between 50° C. and 70° C. while in the heated holding tank.

12. The method of claim 1 , wherein the moistened cellulosic feedstock enters the heated holding tank at a first temperature, and exits the heated holding tank at a second temperature higher than the first temperature.

13. The method of claim 12 , wherein the first temperature is below 50° C., and the second temperature is between 50° C. and 70° C.

14. The method of claim 1 , wherein step c) comprises withdrawing cellulosic feedstock from essentially the entirety of the at least one outlet.

15. The method of claim 1 , further comprising monitoring a temperature of the moistened cellulosic material in the heated holding tank.

16. The method of claim 15 , further comprising adjusting an amount of heat applied to the heated holding tank based on the temperature of the cellulosic material in the heated holding tank.

17. The method of claim 1 , further comprising conveying the cellulosic feedstock through a water impregnator wherein water is added to increase the moisture content of the cellulosic feedstock from less than 15 wt % to 30 wt % to 60 wt %.

18. The method of claim 1 , wherein the hydrolysis comprises the use of a steam explosion reactor.

19. A method for preparing a cellulosic feedstock comprising:

(a) treating a starting cellulosic feedstock in an impregnator with water and obtaining a moistened cellulosic feedstock;

(b) passing the moistened cellulosic feedstock through a heated holding tank, the heated holding tank comprising (i) at least one sidewall defining a passage having an upper portion and a lower portion, (ii) at least one inlet adjacent to the upper portion, and (iii) at least one outlet adjacent the lower portion, wherein the holding tank has a longitudinal axis and at least one of the at least one sidewalls diverges from the longitudinal axis from the upper portion to the lower portion;

(c) withdrawing heated moistened cellulosic feedstock from the at least one outlet of the heated holding tank, wherein the cellulosic feedstock is maintained at a temperature of between 50° C. and 70° C. while in the heated holding tank; and,

(d) subsequently conveying the cellulosic feedstock to a steam explosion reactor.

20. The method of claim 19 , wherein the moisture content of the cellulosic feedstock is increased from less than 15 wt % to 30 wt % to 60 wt % in the impregnator.

21. The method of claim 19 , wherein the moisture content is between 45 wt % and 55 wt%.

22. The method of claim 19 , wherein step (b) comprises passing the cellulosic feedstock downwardly through the heated holding tank.

Assignments (9)
SECURITY INTEREST Recorded Feb 15, 2016
From: ABENGOA BIOENERGY NEW TECHNOLOGIES, LLC
To: ARMSTRONG TEASDALE LLP
Reel/Frame 037734/0948 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Apr 7, 2014
From: NGUYEN, QUANG A.
To: ABENGOA BIOENERGY NEW TECHNOLOGIES, LLC
Reel/Frame 032619/0447 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jul 17, 2013
From: MASCOMA CANADA INC.
To: ABENGOA BIOENERGY NEW TECHNOLOGIES, LLC
Reel/Frame 030816/0512 →
RELEASE OF SECURITY INTEREST Recorded Jun 13, 2013
From: PINNACLE VENTURES, L.L.C.
To: MASCOMA CORPORATION
Reel/Frame 030609/0831 →
RELEASE OF SECURITY INTEREST Recorded Jun 13, 2013
From: KJSB MERGER SUB, INC.
To: MASCOMA CORPORATION
Reel/Frame 030609/0850 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Sep 14, 2012
From: SUNOPTA BIOPROCESS INC.
To: MASCOMA CANADA INC.
Reel/Frame 028961/0812 →
GRANT OF SECURITY INTEREST IN PATENTS Recorded Aug 7, 2012
From: MASCOMA CANADA INC.
To: KJSB MERGER SUB, INC.
Reel/Frame 028739/0237 →
SECURITY AGREEMENT Recorded Jun 22, 2012
From: MASCOMA CANADA INC.
To: PINNACLE VENTURES, L.L.C.
Reel/Frame 028429/0423 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jul 29, 2008
From: BURKE, MURRAY J.; HILLIER, SUNALIE N.
To: SUNOPTA BIOPROCESS INC.
Reel/Frame 021307/0327 →
Priority Claims (1)
CA 2638150 · Jul 24, 2008 · national
Continuity (1)
Related Publication 20100024806A1 · Feb 4, 2010