ANHYDROUS AMMONIA TREATMENT FOR IMPROVED MILLING OF BIOMASS

• US 20120187228A1
• Filed: 07/19/2011
• Published: 07/26/2012
• Est. Priority Date: 07/21/2010
• Status: Active Grant

• Current Assignee: Sustainable Technology Corporation
• Original Assignee: E. I. du Pont de Nemours and Company (Corteva, Inc.)
• Inventors: CAMP, CARL E., DINER, BRUCE A., Fan, Janine, CIRAKOVIC, JELENA
• Granted Patent: US 8,651,403 B2
• Time in Patent Office: Days
• US Class Current: 241/30
• CPC Class Codes: C08H 8/00 Macromolecular compounds derived from lignocellulosic materials pretreatment thereof B27N
• CPC Class Codes: C12P 19/00 Preparation of compounds containing saccharide radicals ketoaldonic acids C12P7/58
• CPC Class Codes: C12P 2201/00 Pretreatment of cellulosic or lignocellulosic material for subsequent enzymatic treatment or hydrolysis
• CPC Class Codes: C12P 7/10 substrate containing cellulosic material
• CPC Class Codes: D21C 3/02 with inorganic bases or alkaline reacting compounds, e.g. sulfate processes
• CPC Class Codes: D21C 5/00 Other processes for obtaining cellulose, e.g. cooking cotton linters obtaining fibres for spinning D01C; Processes characterised by the choice of cellulose-containing starting materials
• CPC Class Codes: Y02E 50/10 Biofuels, e.g. bio-diesel

Abstract

Mechanical milling of biomass as a pretreatment to render the biomass readily saccharifiable requires high energy input. Preceding mechanical milling by treatment with anhydrous ammonia was found to greatly reduce the energy requirement for fine milling, providing a more economical pretreatment process for commercial use.

Claims

1. A process for producing readily saccharifiable biomass comprising:

a) providing lignocellulosic biomass;

b) contacting the biomass of (a) with anhydrous ammonia to produce ammonia-treated biomass; and

c) disrupting the ammonia-treated biomass of (b) by applying mechanical energy through a mechanical disruption means to produce a pretreated biomass which is readily saccharifiable;

wherein the pretreated biomass comprises an amorphous cellulose component and;

wherein the percentage of the amorphous cellulose component in the pretreated biomass is higher as compared with the percentage of the amorphous cellulose component in a pretreated biomass not contacted with anhydrous ammonia and disrupted with the same level of mechanical energy as in (c).

2. The process according to claim 1 wherein the pretreated biomass of step c) has a particle size of less than about 0.1 mm.

3. The process according to claim 1 wherein the energy required for the mechanical disruption of step (c) is about 4 to about 10 fold less as compared with the energy required for mechanical disruption of a lignocellulosic biomass not contacted with anhydrous ammonia.

4. The process according to claim 1 wherein, upon saccharification, the pretreated biomass of step c) produces fermentable sugars at a higher rate when compared with a pretreated biomass that is not contacted with anhydrous ammonia and is disrupted as in (c).

5. The process of claim 1 wherein the ammonia-treated biomass is substantially dry following ammonia pretreatment.

6. The process of claim 1 wherein the mechanical disruption means is selected from the group consisting of a means for:

pounding, grinding, shearing, crushing, and combinations thereof.

7. The process of claim 1 wherein the mechanical disruption means is a means selected from the group consisting of:

attritor milling, hammer milling, ball milling, bead milling, vibratory ball milling, vibratory rod milling, jet milling, pin milling, turbine milling, air classifier milling, roll milling and planetary ball milling.

8. The process of claim 1 wherein steps (b) and (c) occur concurrently.

9. The process of claim 1 wherein the disruption occurs over a period of less than 2 days.

10. The process of claim 9 wherein the disruption occurs over a period of less than 60 minutes.

11. The process of claim 1 wherein the anhydrous ammonia of step (b) is at a concentration that is between about 2 and about 30 weight percent relative to dry weight of lignocellulosic biomass.

12. The process of claim 11 wherein anhydrous ammonia is at a concentration of between about 10 and about 25 weight percent relative to dry weight of lignocellulosic biomass.

13. The process of claim 1 wherein the lignocellulosic biomass of step (b) is in contact with anhydrous ammonia for a period of about thirty minutes to about one year.

14. The process of claim 1 wherein the lignocellulosic biomass of step (b) attains a moisture content of about 15% and about 30% prior to the application of mechanical energy.

15. The process of claim 1 wherein the lignocellulosic biomass of step (b) is contacted with anhydrous ammonia at a temperature that is between about 0°

C. and about 200°

C.

16. The method of claim 1 wherein lignocellulosic biomass of (a) is selected from the group consisting of corn cobs, corn husks, corn stover, grasses, wheat straw, barley straw, hay, rice straw, switchgrass, waste paper, sugar cane bagasse, sorghum bagasse or stover, soy stover, components obtained from milling of grains, trees, branches, roots, leaves, wood chips, sawdust, shrubs, bushes, vegetables, fruits, flowers, animal manure, and a combination thereof.