Combined dry-wet milling process for refining corn

Claim 2

A continuous corn refining process, which comprises: (A) dry milling whole grain corn to provide (a) an endosperm fraction, (b) a germ fraction, (c) a fiber (hull) fraction, and (d) a cleanings fraction; (B) wet milling the endosperm fraction of (A)(a) by sequentially (i) steeping the endosperm fraction, (ii) separating the larger wet endosperm particles from the smaller wet endosperm particles, (iii) milling the larger wet endosperm particles to reduce their particle size, (iv) recombining the wet endosperm particles of (ii) and (iii) into a single fraction, and (v) steeping the endosperm fraction again to provide a mill starch slurry; (C) separating fine fiber tailings from the mill starch slurry of (B)(v); (D) separating the defibered mill starch slurry of (C) into a starch-rich fraction and a protein-rich fraction; (E) concentrating the protein-rich fraction of (D); (F) directly combining each of the fiber (hull) fraction and the cleanings fractions of (A), the fine fiber tailings fraction of (C) and the protein-rich concentrate of (E) without removing any corn oil therefrom, with the germ fraction of (A) to provide a wet animal feed product; and (G) drying the wet feed product of (F) to obtain a final animal feed product.

Claim 3

The process of claim 1 wherein corn oil is separated from the corn germ fraction of (A).

Claim 4

The process of claim 1 wherein corn oil is not separated from the corn germ fraction of (A).

Claim 5

The process of claim 1 wherein in wet milling step (B), the initial weight ratio of the process (steep) water to the endosperm particles is in the range of from about 6:1 to about 7:1.

Claim 6

The process of claim 1 wherein the first steeping step (B)(i) and the second steeping step (B)(v) are conducted in an aqueous medium at an acid or alkaline pH.

Claim 7

The process of claim 5 wherein the steeping medium is acidic.

Claim 8

The process of claim 6 wherein the steeping medium comprises a solution of sulfur dioxide in water.

Claim 9

The process of claim 5 wherein the steeping medium is alkaline.

Claim 10

The process of claim 8 wherein the steeping medium comprises a solution of sodium hydroxide in water.

Claim 11

The process of claim 1 wherein the total residence time of the endosperm particles in steeping steps (B)(i) and (B)(v) is in the range of from about 2 to about 6 hours.

Claim 12

The process of claim 1 wherein in milling step (B)(iii) endosperm particles having a size of greater than about 50 to about 75 microns are reduced in size to about 50 to about 75 microns or less.

Claim 13

The process of claim 1 wherein step (D) is conducted by passing the mill starch slurry through a plurality of hydroclones.

Claim 14

The process of claim 12 wherein the mill starch slurry has a specific gravity of from about 7° to about 9° Baume.

Claim 15

A continuous corn refining process, which comprises: (A) dry milling whole grain corn to provide (a) an endosperm fraction, (b) a germ fraction, (c) a fiber (hull) fraction, and (d) a cleanings fraction; (B) wet milling the endosperm fraction of (A)(a) by sequentially (i) steeping the endosperm fraction in a solution of sulfur dioxide in water, the initial weight ratio of the process (steep) water to the endosperm particles being in the range of from about 6:1 to about 7:1, (ii) separating the wet endosperm particles having a size of greater than about 50 microns from the smaller wet endosperm particles, (iii) impact milling the wet endosperm particles having a size of greater than about 50 microns to reduce their particle size to about 50 microns or less, (iv) recombining the wet endosperm particles of (ii) and (iii) into a single fraction, and (v) steeping the endosperm fraction again in a solution of sulfur dioxide in water to provide a mill starch slurry, the total residence time of steeping steps (i) and (v) combined being in the range from about 2 to about 6 hours; (C) separating the fine corn fiber tailings from the mill starch slurry of (B)(v); (D) passing the defibered mill starch slurry of (C), having a specific gravity of from about 7° to about 9° Baume, through a plurality of hydroclones to provide an underflow stream comprising a starch-rich fraction and an overflow stream comprising a protein-rich fraction; (E) concentrating the protein-rich fraction of (D); (F) directly combining each of the fiber (hull) fraction and the cleanings fraction of (A), the fine fiber tailings fraction of (C) and the protein-rich concentrate of (E) without removing any corn oil therefrom, with the germ fraction of (A) to provide a wet animal feed product; and (G) drying the wet feed product of (F) to obtain a final feed product.

Claim 16

A continuous corn refining process, which comprises: (A) dry milling whole grain corn to provide (a) an endosperm fraction, (b) a germ fraction, (c) a fiber (hull) fraction, and (d) a cleanings fraction; (B) wet milling the endosperm fraction of (A)(a) by sequentially (i) steeping the endosperm fraction in a solution of sulfur dioxide in water, the initial weight ratio of the process (steep) water to the endosperm particles being in the range of from about 6:1 to about 7:1, (ii) separating the wet endosperm particles having a size of greater than about 50 microns from the smaller wet endosperm particles, (iii) impact milling the wet endosperm particles having a size of greater than about 50 microns to reduce their particle size to about 50 microns or less, (iv) recombining the wet endosperm particles of (ii) and (iii) into a single fraction, and (v) steeping the endosperm fraction again in a solution of sulfur dioxide in water to provide a mill starch slurry, the total residence time of steeping steps (i) and (v) combined being in the range from about 2 to about 6 hours; (C) separating the fine corn fiber tailings from the mill starch slurry of (B)(v); (D) passing the defibered mill starch slurry of (C), having a specific gravity of from about 7° to about 9° Baume, through a plurality of hydroclones to provide an underflow stream comprising a starch-rich fraction and an overflow stream comprising a protein-rich fraction; (E) concentrating the protein-rich fraction of (D); (F) directly combining each of the fiber (hull) fraction and the cleanings fraction of (A), the fine fiber tailings fraction of (C) and the protein-rich concentrate of (E) without removing any corn oil therefrom, with the germ fraction of (A) to provide a wet animal feed product; and (G) drying the wet feed product of (F) to obtain a final feed product.

Claim 17

The process of claim 14 wherein corn oil is separated from the germ fraction of (A).

Claim 18

The process of claim 14 wherein corn oil is not separated from the germ fraction of (A).