ETHANOL PRODUCTION SYSTEM AND METHOD

Abstract

A system and method for producing ethanol from dry-milled corn or other grains includes the steps of separating fiber components and embedded starch components from the grain. The fiber components and embedded starch components are cooked at high temperatures and fermented to produce ethanol.

Claims

1. A system for producing ethanol from grain in an ethanol plant, which system includes: a screening device configured for separating fiber components of the grain from other components; and a cooking device configured for cooking ground corn and other starch-containing materials at high temperatures for greater efficiency in producing ethanol by first removing the fiber components of the grain and removing embedded starch components for fermentation to ethanol.

2. The system according to claim 1, which includes: a flour screen configured for receiving ground grain from the ethanol plant; and said flour screen configured for separating said ground grain into multiple components for processing.

3. The system according to claim 2, which includes said flour screen configured for separating said ground grain into: unground corn for removal and return to the plant; fine particulate flour configured for passing through the flour screen, and feeding to a flour mix tank; fine particulate flour configured for passing through the flour screen, and feeding to a flour mix tank; and process water from the existing plant mixed with flour to produce a flour slurry pumped to a slurry mixer.

4. The system according to claim 3, which includes: a fiber mix tank configured for receiving wherein said flour screen is configured for diverting particulate fiber components separated by the flour screen to a fiber mix tank.

5. The system according to claim 4, wherein said plant includes a source of process water.

6. The system according to claim 5, wherein said process water is mixed with said fiber components to produce a fiber slurry.

7. The system according to claim 6, wherein said fiber slurry is at about 20%-40% wt solids.

8. The system according to claim 7, which includes: a jet cooker; said jet cooker is configured to receive steam from said plant; and said jet cooker is configured for mixing fiber slurry.

9. The system according to claim 8 wherein said slurry is heated to a temperature greater than 220° F.

10. The system according to claim 9, which includes: a high temperature cook tube configured to receive the slurry.

11. The system according to claim 10 wherein said slurry in said cook tube is maintained at a temperature above 220° F. for 5 to 15 minutes.

12. The system according to claim 11, which includes: a slurry mixer configured for receiving cooked fiber from said cook tube; and said slurry mixer is configured for blending said cooked fiber and said flour slurry to produce a stream of warm slurry.

13. The system according to claim 12 wherein: said slurry mixer is configured to maintain said stream of warm slurry at a temperature in the range of 160° F. to 210° F.; and said slurry mixer is configured to send said stream of warm slurry to the plant.

14. A system for producing ethanol from grain in an ethanol plant, which system includes: a screening device connected to said ethanol plant and configured for separating fiber components of the grain from other components; a cooking device connected to said screening device and configured for cooking ground corn and other starch-containing materials received from said screening device at high temperatures for greater efficiency in producing ethanol by first removing the fiber components of the grain and removing embedded starch components for fermentation to ethanol; a flour screen connected to said cooking device and configured for: receiving ground grain from the ethanol plant; separating said ground grain into multiple components for processing, including: unground corn for removal and return to the plant; fine particulate flour configured for passing through the flour screen and feeding to a flour mix tank; fine particulate flour configured for passing through the flour screen and feeding to a flour mix tank; a slurry mixer configured for receiving process water from the existing plant and mixing said process water with flour to produce a flour slurry; a fiber mix tank configured for receiving said flour slurry and diverting particulate fiber components separated by the flour screen to said fiber mix tank; a jet cooker configured to receive steam from said plant; said jet cooker is configured for mixing fiber slurry; and a high temperature cook tube configured to receive the slurry.

15. The system according to claim 14 wherein said slurry in said cook to is maintained at a temperature above 220° F. for 5 to 15 minutes.

16. The system according to claim 15, which includes: a slurry mixer configured for receiving cooked fiber from said cook tube; and said slurry mixer is configured for blending said cooked fiber and said flour slurry to produce a stream of warm slurry.

17. The system according to claim 14 wherein: said slurry mixer is configured to maintain said stream of warm slurry at a temperature in the range of 160° F. to 210° F.; and said slurry mixer is configured to send said stream of warm slurry to the plant.

18. A method for producing ethanol from grain in an ethanol plant, which method includes the steps of: providing a screening device configured for separating fiber components of the grain from other components; and providing a cooking device configured for cooking ground corn and other starch-containing materials at high temperatures for greater efficiency in producing ethanol by first removing the fiber components of the grain and removing embedded starch components for fermentation to ethanol.

19. The method according to claim 18, which includes the additional steps of: providing a flour screen configured for receiving ground grain from the ethanol plant; and configuring said flour screen for separating said ground grain into multiple components for processing.

20. The method according to claim 19, which includes the additional steps of: separating with said flour screen said ground grain into unground corn for removal and return to the plant and fine particulate flour configured for passing through the flour screen; passing said fine particulate flour through the flour screen; feeding said fine particulate flour to a flour mix tank; passing said fine particulate flour through the flour screen; mixing process water from the ethanol plant with flour to produce a flour slurry; and pumping said flour slurry to a slurry mixer.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

[0008] The drawings constitute a part of this specification and include exemplary embodiments of the present invention and illustrate various objects and features thereof.

[0009] FIG. 1 is a schematic diagram of a system for producing ethanol from grain embodying an aspect of the present invention.

DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENT

I. Introduction and Environment

[0010] As required, detailed aspects of the present invention are disclosed herein; however, it is to be understood that the disclosed aspects are merely exemplary of the invention, which may be embodied in various forms. Therefore, specific structural and functional details disclosed herein are not to be interpreted as limiting, but merely as a basis for the claims and as a representative basis for teaching one skilled in the art how to variously employ the present invention in virtually any appropriately detailed structure.

[0011] Certain terminology will be used in the following description for convenience in reference only and will not be limiting. The words, “inwardly” and “outwardly” refer to directions toward and away from, respectively, the geometric center of the aspect being described and designated parts thereof. Said terminology will include the words specifically mentioned, derivatives thereof and words of similar meaning.

II. Preferred Embodiment Ethanol Production System and Method

[0012] Ground corn 105, diverted from an existing plant 50, is fed to a flour screen 100 with sufficient screens to allow for separation of the ground corn 105 into three separate components. Unground corn 130, will be removed and sent back to the plant 50. Fine particulate flour 110 will pass through the screens and is fed to a flour mix tank 200. Process water 205 from the existing plant 50 is mixed with the flour to produce a flour slurry, 210, at about 30% wt solids. The flour slurry 210 is pumped to the slurry mixer 600.

[0013] Larger particulate fiber components, which are shown at 120, are separated by the flour screen 100 and diverted to a fiber mix tank 300. Process water 305, from the existing plant 50, is mixed with the fiber components 120 to produce a fiber slurry 310 at about 30% wt solids. The fiber slurry 310, is pumped and fed to a high temperature jet cooker 400, where high pressure steam 405, from the existing plant 50, is mixed with the fiber slurry 310, to produce a high temperature slurry 410 at above 250° F.

[0014] The high temperature slurry 410 is fed to a high temperature cook tube 500, where the mixture will be kept at above 250° F. for approximately 10 minutes. After being held in the high temperature cook tube 500, the cooked fiber 510 will be fed to the slurry mixer 600 where the cooked fiber 510 is blended with the flour slurry 210 to produce a stream of warm slurry 610 at approximately 185° F., which is sent to the existing ethanol plant 50.

[0015] It is to be understood that while certain embodiments and/or aspects of the invention have been shown and described, the invention is not limited thereto and encompasses various other embodiments and aspects.