Method of separating components from a gas stream

• US 8,394,177 B2
• Filed: 06/01/2010
• Issued: 03/12/2013
• Est. Priority Date: 06/01/2010
• Status: Active Grant

• Current Assignee: MBI International
• Original Assignee: The Michigan Biotechnology Institute
• Inventors: Campbell, Timothy J., Teymouri, Farzaneh, Jones, David K.
• Primary Examiner(s): Smith, Duane
• Assistant Examiner(s): Jones, Christopher P
• Application Number:
  US12/791,703
• Publication Number:
  US 20110290114A1
• Time in Patent Office: 1,015 Days
• Field of Search: 95/90, 951/28, 951/39, 951/48, 435/183, 435/277, 127/37
• US Class Current: 95/90
• CPC Class Codes: B01D 53/84 Biological processes
• CPC Class Codes: C12P 2201/00 Pretreatment of cellulosic or lignocellulosic material for subsequent enzymatic treatment or hydrolysis
• CPC Class Codes: Y02A 50/20 Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters

Abstract

This invention provides methods for separating gas components from a gas stream. The methods are particularly advantageous in that an environmentally friendly biomass absorbent is used to assist in the separation process. The invention is particularly suited to separate water soluble gas components from a gas stream. The water soluble gas components can be used to condition the biomass for additional use, such as a conditioned feed for a biofuel. In general, the conditioned biomass will have increased enzyme digestibility, making the conditioned biomass highly suitable as feedstock for biofuel production.

Claims

1. A method of removing at least one gas component of a gas stream to produce a conditioned cellulosic material, comprising:

sending a feed gas stream comprised of a water soluble gas component having a Henry'"'"'s Law constant (K_H) at 25°

C. of at least 0.002 mole/L-atm and a water insoluble gas component having a Henry'"'"'s Law constant (K_H) at 25°

C. of less than 0.002 mole/L-atm to contact cellulosic material within a vessel;

retaining at least a portion of the water soluble gas component within the vessel, as the water insoluble gas component of the feed gas stream is flowed through the vessel, to produce a conditioned cellulosic material having increased enzyme digestibility, wherein the conditioned cellulosic material having increased enzyme digestibility is a cellulosic material that is more readily converted to its constituent sugar components by hydrolytic enzymes relative to that of the cellulosic material initially supplied to the vessel;

collecting an effluent stream from the vessel depleted in concentration of the water soluble gas component;

ceasing collection of the effluent gas stream and sending a purge gas stream different in composition from that of the feed gas stream to the vessel to remove at least a portion of the water soluble gas component retained within the vessel; and

removing the conditioned cellulosic material from the vessel.

2. The method of claim 1, wherein the collection of the effluent gas stream is ceased at a condition in which concentration of the water soluble gas component in the effluent stream becomes greater than a predetermined quantity.

3. The method of claim 2, wherein the collection of the effluent as stream is ceased at a point at which the effluent steam contains at least 0.1 mass % of the water soluble gas component, based on total mass of the effluent stream.

4. The method of claim 1, wherein the collection of the effluent gas stream is ceased at a condition at which temperature of the effluent stream is greater than that of the influent gas.

5. The method of claim 1, wherein the purge gas stream is comprised of at least 90 mass % water insoluble gas.

6. The method of claim 1, wherein the water soluble gas component is a base gas.

7. The method of claim 6, wherein the base gas is selected from the group consisting of ammonia, alkyl amines and pyridine.

8. The method of claim 1, wherein the water soluble gas component is an acid gas.

9. The method of claim 8, wherein the acid gas is selected from the group consisting of water soluble acid gases include, but are not limited to, nitric acid, hydrogen chloride, hydrogen peroxide, formaldehyde, acetic acid, nitrous acid, sulfur dioxide, hydrogen sulfide, carbon dioxide, carbon disulfide, hydrogen cyanide, carbonyl sulfide, methyl mercaptan and ethyl mercaptan.

10. The method of claim 1, wherein the feed as stream has a water soluble gas concentration of at least 1 mass %, based on total weight of the feed gas stream.

11. The method of claim 1, wherein the feed gas stream has a water insoluble gas concentration of at least 10 mass %, based on total weight of the feed gas stream.

12. The method of claim 1, wherein the water soluble gas component retained within the vessel increases enzyme digestibility of the cellulosic material by at least 5%.

13. The method of claim 1, wherein the cellulosic material contains at least 10 wt % water, based on total weight of the cellulosic material.