Biomass treatment for hyperthermal hydrocatalytic conversion

Patent metadata

Field	Value
Publication number	US-9708763-B2
Application number	US-201615190429-A
Country	US
Kind code	B2
Filing date	Jun 23, 2016
Priority date	Dec 18, 2013
Publication date	Jul 18, 2017
Grant date	Jul 18, 2017

Abstract

A selective removal of metal and its anion species that are detrimental to subsequent hydrothermal hydrocatalytic conversion from the biomass feed prior to carrying out catalytic hydrogenation/hydrogenolysis/hydrodeoxygenation of the biomass in a manner that does not reduce the effectiveness of the hydrothermal hydrocatalytic treatment while minimizing the amount of water used in the process is provided.

First claim

What is claims is:

1. A method for selective removal of detrimental metals and their anion species from a cellulosic biomass solids, said method comprising a plurality of vessels:
a. providing each of said vessels with one of detrimental species-containing cellulosic biomass solids;
b. introducing a first dispersed or semi-continuous liquid phase comprising an acidic solution having a pH of at most 4 from an inlet into a first vessel of said plurality of vessel wherein the cellulosic biomass solids in the first vessel is contacted by said first dispersed or semi-continuous liquid phase and first continuous gas phase at a temperature in the range of about 0° C. to about 60° C. wherein the flux of the first liquid phase is at least 1 kg/(m 2 s);
c. repeating step (b) for a second vessel of said plurality of vessels;
d. introducing a second dispersed or semi-continuous liquid phase comprising an aqueous solution having a pH of at least 5 from an inlet into said first vessel of said plurality of vessels treated according to step (b) wherein said acidic solution-treated cellulosic biomass solids in the first vessel is contacted by said second dispersed or semi-continuous liquid phase and second continuous gas phase wherein the flux of the second liquid phase is at least 1 kg/(m 2 s) and discharging an acidic effluent;
e. repeating step (d) for the second vessel of said plurality of vessels treated according to step (c);
f. introducing a third dispersed or semi-continuous liquid phase comprising a base solution having a pH of greater than 9 from an inlet into said first vessel of said plurality of vessels treated according to step (d) wherein said aqueous solution-treated cellulosic biomass solids in the first vessel is contacted by said third dispersed or semi-continuous liquid phase and third continuous gas phase wherein the flux of the third liquid phase is at least 1 kg/(m 2 s) and discharging an aqueous effluent;
g. repeating step (f) for a second vessel of said plurality of vessels treated according to step (e);
h. introducing a fourth dispersed or semi-continuous liquid phase comprising an aqueous solution having a pH of at most 8 from an inlet into said first vessel of said plurality of vessels treated according to step (f) wherein said base solution-treated cellulosic biomass solids in the first vessel is contacted by said fourth dispersed or semi-continuous liquid phase and fourth continuous gas phase wherein the flux of the fourth liquid phase is at least 1 kg/(m 2 s) and discharging a basic effluent;
i. repeating step (h) for the second vessel of said plurality of vessels treated according to step (g);
j. transferring at least a portion of the biomass treated according to steps (h) and (i) to a digestion and/or reaction vessel;
k. wherein at least 2 of the vessels are undergoing at least one of the steps (b) through (j) at the same time; and
l. wherein the amount of the total discharged acidic effluent and basic effluent from the plurality of vessels is in the range of from about 3 parts to about 0.5 parts relative to about 1 part of detrimental species-containing cellulosic biomass solids (dry basis).

2. The method of claim 1 wherein steps (b), (d), (f), (h), or (j) are repeated for n vessels where n is an integer from 2 to 20.

3. The method of claim 2 wherein n is an integer from 2 to 10.

4. The method of claim 3 wherein n is an integer from 3 to 6.

5. The method of claim 1 wherein the first dispersed or semi-continuous liquid phase, is recycled at least one time through the first vessel for step (b) and through the second vessel for step (c).

6. The method of claim 1 wherein the second dispersed or semi-continuous liquid phase, is recycled at least one time through the first vessel for step (d) and through the second vessel for step (e).

7. The method of claim 1 wherein the acidic effluent is discharged until the pH is greater than 3 or until the amount of the acidic effluent exceeds the acidic solution introduced into the vessel, and at least a portion of the subsequent aqueous effluent is recycled at least one time through the first vessel.

8. The method of claim 7 wherein at least a portion of the subsequent aqueous effluent is recycled as the acidic solution.

9. The method of claim 8 further adjusting the pH of at least a portion of the subsequent aqueous effluent to a pH of at most 4 by adding an acid to the discharged aqueous solution prior to recycling as a portion of the acidic solution.

10. The method of claim 1 wherein the third dispersed or semi-continuous liquid phase, is recycled at least one time through the first vessel for step (f) and through the second vessel for step (g).

11. The method of claim 1 wherein the fourth dispersed or semi-continuous liquid phase, is recycled at least one time through the first vessel for step (h) and through the second vessel for step (i).

12. The method of claim 1 wherein the basic effluent is discharged until the pH is less than 9 or until the amount of the basic effluent exceeds the base solution introduced into the vessel, and at least a portion of the subsequent aqueous effluent is recycled at least one time through the first vessel.

13. The method of claim 12 wherein at least a portion of the subsequent aqueous effluent is recycled as the base solution.

14. The method of claim 13 further adjusting the pH of at least a portion of the subsequent aqueous effluent to a pH of greater than 9 by adding a base to the discharged aqueous solution prior to recycling as a portion of the base solution.

15. The method of claim 1 wherein, in the digestion and/or reaction zone, the treated cellulosic biomass is contacted with a hydrothermal hydrocatalytic catalyst in the presence of hydrogen and a digestion solvent thereby producing an intermediate oxygenated product stream comprising oxygenated hydrocarbons and water; and at least a portion of the water is separated and recycled as the aqueous solution.

16. The method of claim 1 wherein, in the digestion and/or reaction zone, the treated cellulosic biomass is contacted with a hydrothermal hydrocatalytic catalyst in the presence of hydrogen and a digestion solvent thereby producing an intermediate oxygenated product stream; at least a portion of the oxygenated intermediate product stream is converted to a hydrocarbon product stream comprising hydrocarbons and water; and at least a portion of the water is separated and recycled as the aqueous solution.

17. The method of claim 15 wherein, the oxygenated intermediate product stream comprises oxygenated hydrocarbons and water, and at least a portion of the water is separated and recycled as the aqueous solution.

Assignees

• Shell Oil Co

Inventors

• Powell Joseph Broun
• Chheda Juben Nemchand

Classifications

• C10G2300/4081

  Recycling aspects · CPC title

• C10G1/065

  in the presence of a solvent · CPC title

• C10G2300/205

  Metal content · CPC title

• Y02P30/20

  using bio-feedstock · CPC title

• C10G2300/1014

  of vegetal origin · CPC title