Method of treating lignocellulose materials to produce ruminant feed

• US 4,136,207 A
• Filed: 01/24/1977
• Issued: 01/23/1979
• Est. Priority Date: 01/24/1977
• Status: Expired due to Term

• Current Assignee: Stage Technologies Incorporated
• Original Assignee: Stage Technologies Incorporated
• Inventors: Bender, Robert
• Primary Examiner(s): Corbin, Arthur L.
• Application Number:
  US05/762,095
• Time in Patent Office: 729 Days
• Field of Search: 426/635, 426/636, 426/447, 426/453, 426/454, 426/455, 426/456, 426/465, 426/472, 426/481, 426/510, 426/511, 426/512, 426/520, 426/523, 426/807, 162/18, 162/21, 162/68, 127/37
• US Class Current: 426/510
• CPC Class Codes: A23K 10/32 from hydrolysates of wood or straw
• CPC Class Codes: Y10S 426/807 Poultry or ruminant feed

Abstract

Lignocellulose material is mechanically compacted and subjected to sudden pressure increase by exposure to saturated steam in a digestor vessel in the absence of added chemical reagents to obtain a cooked material which is then mechanically compacted while under said saturated steam pressure. Small portions of the cooked and mechanically compacted material are thereafter subjected to rapid reduction in pressure down to atmospheric pressure and then recovered in a condition of enhanced digestibility by ruminants.

Claims

1. A process for preparing cellulosic material of enhanced digestibility by ruminants, which comprises the steps of:

initially mechanically compacting a lignocellulose material selected from the group consisting of hardwood wood chips and sawdust, said lignocellulose material having a moisture content at or above the fiber saturation point;

continuously feeding the compacted lignocellulose material to a pressure withstanding digestor vessel;

subjecting said compacted lignocellulose material to sudden increase in pressure by exposure to saturated steam, at a pressure of at least 200 psig, in said digestor vessel;

conveying said lignocellulose material through said digester vessel while maintaining said lignocellulose material in contact with saturated steam, at a pressure of at least 200 psig for a period of at least 15 seconds, and in the absence of added chemical reagents other than said steam whereby a cooked and digested ligno-cellulose materials is obtained;

mechanically compacting the cooked and digested lignocellulose material while under said saturated steam pressure of at least 200 psig and adjusting or maintaining the free moisture content thereof at or above the fiber saturation point;

subjecting small portions of the cooked and digested and mechanically compacted lignocellulose material successively in a continuous manner to rapid reduction in pressure down to atmospheric pressure in a time interval of not more than 0.1 secs. resulting in cooling of said material; and

then

continuously recovering said lignocellulose material in a condition of enhanced digestibility by reminants.

2. The process of claim 1, wherein subjection of the small portions of the cooked and digested and mechanically compacted lignocellulose material to rapid reduction in pressure is accomplished on discharge of the material from the digestor vessel.

3. The process of claim 2, wherein saturated steam pressures in the range of 200-310 psig are maintained in the digestor vessel continuously during feeding material to and discharging material from said vessel.

4. The process of claim 3, wherein the lignocellulose material is initially at its entrance to the pressure withstanding digestor vessel to form a dense, compact plug of material.

5. The process of claim 3, wherein said small portions of lignocellulose material are discharged through a narrow, intermittently opening throttle valve into ambient temperature and pressure conditions.

6. The process of claim 5, wherein the lignocellulose material has a moisture content of at least 40% at the time of discharge.

7. The process of claim 3, wherein the lignocellulose material is aspen poplar wood.

8. The process of claim 7, wherein the lignocellulose material is subjected to saturated steam pressures in the range from about 210 to about 250 psig for about 5 to about 20 minutes in said digestor vessel.